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Production of BHD (Bio Hydrofined Diesel) with Improved Cold Flow ...

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Cracking Ratio, mass%<br />

40<br />

35<br />

30<br />

25<br />

20<br />

15<br />

10<br />

5<br />

0<br />

Amorphous Type<br />

Zeolite Type<br />

0 20 40 60 80 100<br />

Isomerization Ratio, mass%<br />

Fig. 7<br />

Relationship between Isomerization and Cracking<br />

The relationship between reaction pressure and feed conversion is shown in Fig. 8. Activity is<br />

higher under low pressure conditions. It is thought that this is because dehydrogenation <strong>of</strong> normal<br />

paraffin, which is the origin <strong>of</strong> the isomerization reaction, occurs more readily at lower pressure.<br />

Feed Conversion, %<br />

Fig. 8<br />

100<br />

80<br />

60<br />

40<br />

20<br />

0<br />

3MPa<br />

6MPa<br />

10MPa<br />

280 300 320 340 360<br />

Reaction Temperature, ℃<br />

Relationship between Reaction Pressure and Feed Conversion<br />

3.3 Properties <strong>of</strong> isomerization products<br />

Table 6 shows the properties <strong>of</strong> the isomerized <strong>BHD</strong> (isomerization ratio: 50%), which was made<br />

by distilling <strong>of</strong>f the fraction lighter than 185°C. The isomerized <strong>BHD</strong> has greatly improved cold flow<br />

properties compared to the normal <strong>BHD</strong>. The cetane number was slightly lower after isomerization,<br />

but the isomerized <strong>BHD</strong> still has a cetane number higher than that <strong>of</strong> conventional diesel oil, and<br />

should have good ignition properties.<br />

Table 6<br />

Properties <strong>of</strong> Isomerized <strong>BHD</strong>

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