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ORNL-4191 - the Molten Salt Energy Technologies Web Site

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about 500 mm Hg at <strong>the</strong> test operating temperature<br />

(1200°F), it will be necessary to maintain an over-<br />

pressure of BF3 in <strong>the</strong> pump bowl vapor space to<br />

avoid a loss of BF3 from <strong>the</strong> salt with <strong>the</strong> resultant<br />

increase in salt liquidus temperature. The cover<br />

gas system is being revised to include <strong>the</strong> neces-<br />

sary equipment for handling and controlling <strong>the</strong><br />

EF3. 'This system, shown schematically in Fig.<br />

'7.4, includes some of <strong>the</strong> features of <strong>the</strong> cover<br />

gas system used with <strong>the</strong> MSRE coolant salt, and<br />

<strong>the</strong> information developed in <strong>the</strong> test will be useful<br />

in planning <strong>the</strong> revisions which will be necessary<br />

to prepare for testing of NaBF4 in <strong>the</strong> MSRE<br />

coolant system.<br />

'The operating conditions for <strong>the</strong> loop are:<br />

Temperature 1200°F<br />

Flow rate 800 gpm<br />

Pump head 120 ft<br />

Pump speed 1800 rpm<br />

The tendency of BF to induce polymerization of<br />

organic materials could cause problems in <strong>the</strong><br />

pump lubrication system and in <strong>the</strong> off-gas line.<br />

The heliuiii purge to <strong>the</strong> shaft annulus will be<br />

adjusted to minimize diffusion of BF, into <strong>the</strong><br />

pump bearing chamber, and filters are provided<br />

in <strong>the</strong> off-gas line to protect <strong>the</strong> pump tank pressure<br />

control valve. The BF3 flow required will be<br />

dictated by <strong>the</strong> total pump bowl pressure, <strong>the</strong><br />

desired BF3 partial pressure, and <strong>the</strong> required<br />

heliuiii purge flow.<br />

It is planned to operate <strong>the</strong> loop iso<strong>the</strong>rmally<br />

for a period of about six months. The objective<br />

will be to uncover any problems associated with<br />

<strong>the</strong> circulation of NaBF4 and to devise and test<br />

suitable solutions or corrective measures.<br />

7.4 MSBR PUMPS<br />

A. G. Grindell<br />

P. G. Smith L. V. Wilson<br />

Survey of Pump Experience Circulating Liquid<br />

Metals and MOltell SlaIt5<br />

A survcy of experience with pumps for liquid<br />

metals and molten salt was made, and a report1<br />

'P. G. Smith, Experience with High-Temperature<br />

Centrifugal Punips in Nuclear Reactors arid Their<br />

Application to <strong>Molten</strong>-<strong>Salt</strong> Thermal Breeder Reactors,<br />

<strong>ORNL</strong>-'1'M-1993 (September 1967).<br />

96<br />

was issued relating pump descriptions, operating<br />

hours, and <strong>the</strong> problems encountered during oper-<br />

ation.<br />

Introduction of MSBW Pump Program<br />

The objectives of <strong>the</strong> salt pump program for <strong>the</strong><br />

MSBR include <strong>the</strong> production of suitable and reliable<br />

pumps for <strong>the</strong> fuel, blanket, and coolant salt<br />

circuits of <strong>the</strong> <strong>Molten</strong>-<strong>Salt</strong> Breeder Experiment<br />

(MSRE) and its nonnuclear prototype, <strong>the</strong> Engineering<br />

Test Unit (ETU). Table 7.2 presents <strong>the</strong><br />

pump requirements as <strong>the</strong>y are presently envisioned.<br />

A single conditional objective requires<br />

that <strong>the</strong> pumps developed for <strong>the</strong> MSBE should be<br />

capable of flow capacity scale-up by a factor of<br />

approximately 4 to <strong>the</strong> 550-Mw (<strong>the</strong>rmal) MSBR<br />

with little or no additional development work.<br />

Our approach is to invite <strong>the</strong> strong participation<br />

of U.S. pump industry in <strong>the</strong> design, development,<br />

and production of <strong>the</strong>se pumps. We will<br />

prepare pump specifications along with a preliininary<br />

pump assembly drawing, pertinent rotordynamic<br />

and heat transfer analyses, and <strong>the</strong> results<br />

of a survey of fabrication methods for suhmission<br />

to pump manufacturers. The pump maiiufacturers<br />

would be asked to make an independent<br />

analysis of <strong>the</strong> pump specifications arid supporting<br />

material and to define all <strong>the</strong> changes and improvements<br />

<strong>the</strong>y believe necessary. Paren<strong>the</strong>tically,<br />

it may prove necessary to pay for several<br />

independent analyses. The pump inaiiufacturers<br />

would <strong>the</strong>n be asked to bid on <strong>the</strong> production of<br />

<strong>the</strong> detailed pump design and shop drawings, <strong>the</strong><br />

fabrication and assembly for shop inspection of<br />

<strong>the</strong> required quantities of sa1.t pumps, and <strong>the</strong><br />

shipment of disassembled pumps to <strong>ORNL</strong> for<br />

fur<strong>the</strong>r testing.<br />

Two important implicit requirements are provided<br />

in this approach. The individual pump<br />

configurations are matched to <strong>the</strong> various MSRE<br />

systems requirements by and at <strong>ORNL</strong>, and <strong>the</strong><br />

responsibility for approval of <strong>the</strong> final pump design<br />

and <strong>the</strong> detailed drawings rests with <strong>ORNL</strong>.<br />

The principal pump components requiring development<br />

effort are <strong>the</strong> molten-salt bearing, if<br />

used, <strong>the</strong> shaft seal, and a full-scale rotor-dynamic<br />

simulator, if supercritical operation of a salt pump<br />

is required, that is, operation of <strong>the</strong> pump at<br />

speeds above <strong>the</strong> first critical shaft speed. The<br />

pump manufacturers would be invited to participate<br />

in this and o<strong>the</strong>r development work <strong>the</strong>y may

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