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1. Introduction - Firenze University Press

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Temperature (°C)<br />

8<br />

7<br />

6<br />

5<br />

4<br />

3<br />

2<br />

1<br />

0<br />

16<br />

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17<br />

Time (min)<br />

79<br />

Internal Temperature<br />

Internal <strong>Press</strong>ure<br />

Fig. 4. <strong>Press</strong>ure and temperature profile with elapsing time for CO2 hydrate formation in SDS 300<br />

ppm- experimental run 2 in Table <strong>1.</strong> Water spraying starts at t = 2 min.<br />

In Fig. 5 pressure profiles for runs 1, 2, 3 in Table 1 are reported. These three runs help to determine<br />

the effects of two different promoters (SDS and THF). It is evident that in absence of promoter,<br />

pressure decreases, due to gas capture in the hydrate structure, are not observable. On the other<br />

hand, in presence of promotor, pressure starts decreasing after 4-5 minutes, with an induction time<br />

shorter than those observed in other experiments described in literature, as already proved in our<br />

previous applications [20].<br />

<strong>Press</strong>ure (bar)<br />

32<br />

31<br />

30<br />

29<br />

28<br />

27<br />

26<br />

no promotor<br />

SDS 300 ppm<br />

THF 1%wt<br />

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16<br />

Time (min)<br />

Fig. 5. <strong>Press</strong>ure profiles with elapsing time for CO2 hydrate formation with and without<br />

promotors- experimental runs 1-2-3 in Table <strong>1.</strong> Water spraying starts at t = 1 min.<br />

Several samples were taken directly from the reactor. Hydrate storage capacity was determined<br />

putting hydrate samples inside a custom-built dissociation vessel, as described in section 2.3.<br />

32<br />

30<br />

28<br />

26<br />

24<br />

22<br />

20<br />

18<br />

<strong>Press</strong>ure (bar)

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