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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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CaBr 2 HYDROLYSIS FOR HBr PRODUCTION USING A DIRECT SPARGING CONTACTOR<br />

Capture/neutralisation <strong>of</strong> product HBr<br />

The product gases containing unreacted steam and HBr leave the reactor through a port in the SS<br />

(or Pyrex glass) flange assembly. The product gases then pass through a heat-traced line, a glass trap,<br />

and a glass condenser (chilled to 12°C) and are collected into a tank containing (10 N) sodium hydroxide<br />

solution for HBr capture. The system is designed so that all gases introduced to it must pass through<br />

the condensate/neutralisation tank, where liquid or gaseous hydrogen bromide is neutralised by the<br />

following reaction:<br />

HBr + NaOH → NaBr + H 2 O (5)<br />

The use <strong>of</strong> a concentrated sodium hydroxide solution (10 N) in sufficient volume to neutralise all<br />

hydrogen bromide product formed during the reaction time ensures that even trace levels <strong>of</strong> HBr will<br />

not be released from the receiver to the vent.<br />

Experimental procedures<br />

Reagent grade anhydrous CaBr 2 (199.888 M.W.) was poured into the melt bath. For start-up and<br />

shutdown, argon, an inert gas, is used to purge the test apparatus. On start-up, argon gas flows at a<br />

rate <strong>of</strong> 1 L/min to remove residual air in the reactor and the rest <strong>of</strong> the system before the temperature<br />

is raised. The presence <strong>of</strong> air (oxygen) in the reactor alters the reaction path and produces bromine<br />

gas. Minor amounts <strong>of</strong> bromine could be detected with potassium iodide-starch test paper from the<br />

opening <strong>of</strong> the gas outlet; this testing showed that no release <strong>of</strong> Br 2 gas was taking place. Argon is also<br />

sparged as fine bubbles in the deionised water for deaerating the feedwater to the steam generator.<br />

At the end <strong>of</strong> the experiment, the steam is shut <strong>of</strong>f and a flow <strong>of</strong> argon gas is started to purge HBr<br />

from the reactor and the rest <strong>of</strong> the system.<br />

Reagent steam is produced at 423 K, 0.525 MPa (5.25 bar). Superheating <strong>of</strong> 50 K takes place in the<br />

feed lines so that the steam enters the Lindberg furnace at about 473 K. The reagent steam is metered<br />

into the reactor by means <strong>of</strong> a metering valve. Significantly, COMSOL TM modelling showed that the<br />

steam would quickly reach the temperature <strong>of</strong> the bath with only a small draw on the heat reservoir.<br />

Success in adopting the approach <strong>of</strong> feeding low temperature steam considerably simplified the<br />

steam feed arrangement, which employed 316 SS up to the connection with the alumina sparger feed<br />

near the top <strong>of</strong> the furnace.<br />

Produced HBr is scrubbed by the use <strong>of</strong> 10 N sodium hydroxide solution to form sodium bromide.<br />

For all the runs, the initial inventory is 1.25 L <strong>of</strong> sodium hydroxide solution. The NaOH solution was<br />

sampled at regular intervals and sent to Argonne’s Analytical Chemistry Laboratory for analysis. Volume<br />

aliquots <strong>of</strong> solution samples were diluted with reagent water and analysed by ion chromatography to<br />

determine bromide. Separate aliquots were diluted with acid addition and analysed by inductively<br />

coupled plasma-atomic emission spectrometry (ICP-AES) to determine calcium. During the data analysis,<br />

adjustments are made for the addition <strong>of</strong> condensed unreacted steam to the neutralisation solution.<br />

Samples <strong>of</strong> molten salts (calcium bromide-calcium oxide melts; ~2 10 –3 L) were collected on a<br />

graphite rod thrust to the bottom <strong>of</strong> the molten salt bath. Melt samples are taken at the beginning <strong>of</strong><br />

the test run before steam is on and at the end <strong>of</strong> test run after steam is shut <strong>of</strong>f and the system is<br />

purged with argon for at least 15 minutes. The melt samples were also collected for analysis. The salt<br />

samples are ground to powder with an agate mortar and pestle under dry nitrogen in a glove-bag<br />

enclosure. To determine the amounts <strong>of</strong> bromide and oxide present in each salt, a portion <strong>of</strong> powder<br />

(50 10 –6 kg) is treated with methanol (3 10 –3 L), which dissolves the CaBr 2 fraction but does not dissolve<br />

CaO. The methanol solvent was filtered using suction through a 2.5 cm diameter, 5-μm pore-size,<br />

Teflon filter (Millipore), and the solids on the filter are washed with additional methanol. The<br />

methanol filtrate is subsequently transferred to a beaker with water and the volume is reduced by<br />

heating to expel the methanol. The remaining water solution is transferred to a volumetric flask and<br />

diluted for analysis by ion chromatography to determine Br in the salt sample. The solids collected on<br />

the filter are dissolved in dilute nitric acid solution, brought to volume in a volumetric flask, and<br />

analysed by ICP-AES to determine calcium, which is assigned as calcium oxide.<br />

NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010 273

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