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ORNL-2106 - the Molten Salt Energy Technologies Web Site

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4.1. HEAT TRANSFER AND PHYSICAL PROPERTIES<br />

ART FUEL-TO-NoK HEAT EXCHANGER<br />

S. 1. Cohen J. L. Wantland<br />

The ART fuel-to-NaK heat exchanger test system1<br />

was modified for fur<strong>the</strong>r studies of heat transfer<br />

and friction characteristics. Six 60-deg staggered<br />

spacers and six &de9 inclined spacers were<br />

placed alternately on <strong>the</strong> tube bundle, and trans-<br />

verse pressure taps were installed across one<br />

spacer of each type. The average transverse<br />

pressure drop across each instrumented spacer<br />

was plotted in terms of <strong>the</strong> ratio of <strong>the</strong> transverse<br />

pressure drop to <strong>the</strong> velocity head times <strong>the</strong> fluid<br />

density over <strong>the</strong> Reynolds modulus range of 3000<br />

to 8000. For <strong>the</strong> inclined spacer this term varied<br />

from 1.4 to 1.1, and for <strong>the</strong> staggered spacer <strong>the</strong><br />

data fell randomly between 0.01 and 0.03, with no<br />

definite trend established. The analytical investi-<br />

gation, referred to previously,2 on a method of<br />

correlating fluid-friction data for flow parallel<br />

to a square array of cylindrical tubes in rectangular<br />

cross-section flow channels was ~ompleted.~<br />

An experimental study is being made of <strong>the</strong><br />

fuel-side fluid-friction characteristics 6f a mockup<br />

of <strong>the</strong> present design of <strong>the</strong> ART fuel-to-NaK<br />

heat exchanger. The dimensions of this apparatus<br />

and <strong>the</strong> spacer configuratibn will simulate <strong>the</strong><br />

ART heat exchanger as nearly as possible, except<br />

that <strong>the</strong>re will be no headers and <strong>the</strong> tube bundle<br />

will not have <strong>the</strong> curvature specified for <strong>the</strong><br />

ART; that is, <strong>the</strong> friction characteristics for a<br />

straight length of tube bundle will be determined.<br />

An experimental heat exchanger has been de-<br />

signed and is now being fabricated that will be<br />

similar to <strong>the</strong> one on which tests were conducted<br />

previously,' with <strong>the</strong> exception that <strong>the</strong> tubes will<br />

be spaced on a triangular array ra<strong>the</strong>r than a<br />

Friction Data /or Tube Bundles of<br />

and Tube Bundle to Shell Wall Spacing,<br />

<strong>ORNL</strong> CF-M-4-162 (April 5, 1956).<br />

'J. L. Wantland, Thennnl Cbnracieristics of <strong>the</strong> ART<br />

Fuel-to-NaK Heat Exchanger, <strong>ORNL</strong> CF-55-12-120<br />

(Dec. 22, 1955).<br />

H. F. Poppendiek<br />

data for direct comparison of <strong>the</strong> heat-transfer<br />

and fluid-friction characteristics of <strong>the</strong> two differ-<br />

ent configurations in <strong>the</strong> transitional Reynolds<br />

modulus range.<br />

ART HYDRODYNAMICS<br />

C. M. Copenhover F. E. Lynch<br />

G. L. MullerS<br />

Sodium Flow in Reflector Cooling Sysfem<br />

A 5/22-scale model of <strong>the</strong> reflector-core shell<br />

cooling annulus and inlet system was designed and<br />

fabricated (Fig. 4.1.1) in order to determine quanti-<br />

tatively <strong>the</strong> flow distribution in <strong>the</strong> annulus and<br />

<strong>the</strong> various pressure drops in <strong>the</strong> sodium system.<br />

The fluid used in <strong>the</strong> model was water at temper-<br />

atures between 20 and SOOC. Although <strong>the</strong> model<br />

does not incorporate <strong>the</strong> reflector cooling holes,<br />

12 nozzles were spaced radially around <strong>the</strong> inlet<br />

header to take off fluid at various sectors of <strong>the</strong><br />

inlet header to mock up flow through <strong>the</strong> cooling<br />

holes.<br />

The flow distribution was studied by three<br />

methods: (1) <strong>the</strong> static pressure measured axially<br />

across <strong>the</strong> annulus in conjunction with <strong>the</strong> total<br />

annulus flow rate measured by a rotameter gave<br />

<strong>the</strong> average velocities through <strong>the</strong> annulus for <strong>the</strong><br />

two positions nearest <strong>the</strong> inlets and <strong>the</strong> two<br />

positions far<strong>the</strong>st away, (2) Pitot-static combi-<br />

nation measurements were obtained at positions<br />

1-3 and 3-3 (Fig. 4.1.1), and (3) high-speed motion<br />

pictures were made of periodic ink injections.<br />

A quantitative measurement of <strong>the</strong> flow distri-<br />

bution was defined as<br />

on v1 + v3<br />

where<br />

Qj = volumetric flow rate in annulus far<strong>the</strong>st<br />

from inlet,<br />

Qn = volumetric flow rate in annulus nearest to<br />

inlet,<br />

. V = average linear velocity at station indicated<br />

by subscript number.<br />

'On assignment from Pratt 8 Whitney Aircraft.<br />

219

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