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Heterogeneously Catalyzed Oxidation Reactions Using ... - CHEC

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5.3 Results<br />

two association sites on benzaldehyde were estimated capable of cross‐associating with water only.<br />

The cross association parameters were estimated with the modified CR‐1 combining rule. Finally, one<br />

cross‐association site was estimated on CO2 to only cross‐associate with benzyl alcohol for the last<br />

system (entry 4). Further details can be found in ref. [29]. Since the model performed satisfactorily<br />

for binary systems, ternary systems were modeled in the next step.<br />

Table 5‐4: Fitted kij and βcross values for binary systems with cross association.<br />

Entry Compound 1 Compound 2 kij<br />

137<br />

βcross<br />

Temperature<br />

range (°C)<br />

1 CO2 H2O 0.15476 0.02362 80<br />

2 H2O Benzyl alcohol 0.00841 0 20 – 150<br />

3 H2O Benzaldehyde ‐0.06387 0.13074 25 – 147<br />

4 CO2 Benzyl alcohol<br />

‐0.063819 +<br />

8.353∙10 ‐4 ∙ T<br />

(K)<br />

0.26337 60 – 180<br />

5.3.3 Application of the CPA equation of state for phase behavior modeling<br />

The binary interaction parameters between the relevant compounds allowed the prediction of the<br />

phase behavior of ternary mixtures, i.e. benzyl alcohol – O2 – CO2 representing the substrate mixture<br />

and benzaldehyde – H2O – CO2 representing the product mixture at 100 % conversion and 100 %<br />

selectivity. The phase behavior predictions were accompanied by measuring dew points<br />

experimentally.<br />

(a) (b)<br />

Figure 5‐3: CPA Equation of State predictions (lines) and experimental data (points) for the phase transitions<br />

of the ternary systems benzyl alcohol – O2 – CO2 (a) and benzaldehyde – H2O – CO2 at catalysis‐relevant<br />

conditions and compositions.

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