Oa. Fedorchenko et al., COMPUTER-SIMULATION OF THE WATER AND HYDROGEN DISTILLATION AND CECE PROCESS AND ITS EXPERIMENTAL-VERIFICATION, Fusion technology, 28(3), 1995, pp. 1485-1490
Mathematical simulation procedures have been developed for three proce
sses of hydrogen isotopes separation: 1) a non steady-state water dist
illation; 2) a cryogenic distillation; 3) combine electrolysis and mul
tistage water/hydrogen catalytic exchange (CECE) process. The simulati
on procedures possess some special features. Thus, the comparatively l
arge step of integration and as a result of this high fast-acting is t
he peculiarity of the model for the dynamic behaviour of water distill
ation column operating at total reflux. The simulation procedure for C
ECE process considers six components and three phases (liquid water, w
ater vapour, and hydrogen gas) and allows to carry out computations fo
r any mole fraction stock. This procedure, as the one for cryogenic di
stillation process, is not based on the Newton-Raphson method, and, in
spite of this, convergence is reached by a small number of iterations
(4-11).