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Panels a e in Fig. 6 show the percentage of conversion as a function of temperature for (a) virgin n-C7 asphaltenes and asphaltenes in the presence of (b) fumed silica, (c) SNi2, (d) SPd2, and (e) SNi1Pd1 nanoparticles at different heating rates of 5, 10, and 20 °C/min.
Figure 5 CO 2 conversion as a function of temperature and pressure.
The decrease in the conversion as a function of time was observed depending on operating conditions.
Open image in new window Fig. 20 Overall conversion as a function of TOS for commercial mordenite catalysts.
Fig. 5 Ammonia to nitrite conversion as a function of cell mass (OD600 nm) for growing cultures of N. europaea[pSK2] and untransformed N. europaea.
Plots of conversion as a function of time are shown in (Fig. 6) for the support (SZ) and supported (5Mo2C/SZ) catalyst.
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Figure 6b shows CO conversions as a function of temperature over the "used" catalysts.
Figure 6a shows CO conversions as a function of reactor bed temperature over the fresh catalysts.
Figure 5 shows the conversions as a function of time on stream for the various metal modified catalysts.
A second-order model was obtained to predict conversions as a function of temperature and catalyst concentration.
SSTIs coated with Pt/γ-Al2O3 showed different kinetics for differential conversions as a function of temperature.
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