A dual temperature hydrogen isotopic exchange reaction system between water and hydrogen gas is numerically analyzed. The system has two features; high efficiency of isotope exchange reaction and operation under atmospheric pressure. To achieve them, the low temperature section of the system is composed of water mist and hydrogen gas co-current reactor units. For the high temperature section, a multistage-type reactor, in which a bubble plate, superheater and catalyst bed are alternatively arranged, is applied.
From a material balance between these reactors, enrichment and decontamination factors for the system are expressed as functions of seven parameters : unit number of the low temperature co-current reactor (
X) ; stage number of the high temperature section (
Y) ; flow ratio of tritium enriched water to decontaminated water (
P/
W), flow ratio of feed water to hydrogen gas (
F/
G) ; reaction temperatures of the low and high temperature sec-tions (
Tc,
Th) ; and bubble plate temperature (
Tb). Numerical calculations show that enrich-ment factor depends remarkably on
F/
G and
Tb as well as
X and
Y.
In order to understand the separation characteristics visually, the McCabe-Thiele diagrams for the present system are drawn and compared with the results calculated.
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