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Nuclear Production of Hydrogen, Fourth Information Exchange ...

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HEAT PUMP CYCLE BY HYDROGEN-ABSORBING ALLOYS TO ASSIST HTGR IN PRODUCING HYDROGEN<br />

Then, the A hydride <strong>of</strong> MaH X is heated from T L to T M , and the Alloy B shown by Mb is heated from<br />

T M to T H . Consequently, the hydrogen equilibrium pressure <strong>of</strong> MaH X rises to p A,M , and that <strong>of</strong> Mb rises<br />

to p B,H . Since it is designed that p A,M is higher than p B,H , hydrogen is transferred from Alloy A to Alloy B.<br />

Heat is supplied to MaH X in order to desorb hydrogen from Alloy A. At the same time, heat is extracted<br />

in hydrogenating Mb to MbH X . In this condition, heat is flowed from the low temperature <strong>of</strong> T M to the<br />

higher temperature <strong>of</strong> T H . Then the B bed remained T H during hydrogenating. The second stage is the<br />

reversal <strong>of</strong> the first stage. After the second stage, Alloys A and B are at the same initial condition <strong>of</strong> the<br />

first stage. Thus, the absorption-desorption cycle is continued, and the heat pump cycle is completed.<br />

The entropy change <strong>of</strong> hydrogen-absorbing alloy is almost constant regardless <strong>of</strong> different alloys.<br />

This means that the intercept along the vertical axis in Figure 5 is almost the same regardless <strong>of</strong><br />

different alloys. In addition, the enthalpy change that means the slope <strong>of</strong> the van’t H<strong>of</strong>f plot in<br />

Figure 5 decreases with the partial displacement <strong>of</strong> V by Fe. Therefore, two alloys comprised in the<br />

heat pump can be found.<br />

Experiment <strong>of</strong> high-temperature heat pump<br />

Temperature enhancement during H 2 absorption<br />

An alloy <strong>of</strong> ZrV 1.9 Fe 0.1 was manufactured from metal ingots <strong>of</strong> Zr, V and Fe in an Ar-arc melting<br />

furnace, and the alloy was crushed and screened between 12 to 32 mesh in an Ar globe box, because<br />

the alloy is flammable in air. The alloy particles <strong>of</strong> 5.012 kg were packed in a dual cylindrical vessel<br />

made <strong>of</strong> SUS-316. After evacuated by a diffusion pump at temperature <strong>of</strong> 600°C, the alloy bed is cooled<br />

or heated to a specified temperature <strong>of</strong> T 0 by the outside electric furnace. After sufficient time,<br />

electricity input to furnace was stopped. At the same time, hydrogen was supplied under a constant<br />

flow rate dented by W. Temperature was measured in several positions in the bed, and it was found<br />

that the temperature was almost uniform in the bed.<br />

Figure 6 shows several experimental results <strong>of</strong> variations <strong>of</strong> temperature in the inside <strong>of</strong> the<br />

ZrV 1.9 Fe 0.1 particle bed with hydrogenating. T is a local temperature, q m is the average hydrogen absorbed<br />

amount in the bed, and q 0 is the saturated absorbed amount after sufficiently long time has elapsed.<br />

The experimental temperatures shown by solid lines increased without any external heating during<br />

hydrogenating.<br />

Figure 6: Temperature enhance factor with hydrogen absorption amount<br />

Figure 7 shows the maximum temperature increase defined by T max -T 0 that is plotted as a<br />

function <strong>of</strong> the inlet temperature <strong>of</strong> T 0 and the hydrogen flow rate <strong>of</strong> W. Heat generated during<br />

hydrogenating <strong>of</strong> ZrV 1.9 Fe 0.1 is consumed for heating hydrogen introduced to the bed and heat leakage<br />

412 NUCLEAR PRODUCTION OF HYDROGEN – © OECD/NEA 2010

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