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

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Isomerized <strong>BHD</strong> <strong>BHD</strong><br />

Density 15℃ g/cm3 0.781 0.783<br />

Viscosity 30℃ mm2/s 3.9 4.1<br />

Pour Point ℃ +5.0 +20.0<br />

Cloud Point ℃ +4 +21<br />

Cetane Number 90.3 101<br />

3.4 Property <strong>of</strong> isomerized <strong>BHD</strong>-blended diesel oil<br />

The isomerized <strong>BHD</strong> described in Table 6 was blended <strong>with</strong> conventional diesel oil, and a variety<br />

<strong>of</strong> mixtures were evaluated. As shown in Table 7, the cold filter plug point (CFPP) <strong>of</strong> diesel oil<br />

containing isomerized <strong>BHD</strong> was lower than that <strong>of</strong> normal <strong>BHD</strong>, even when the isomerized <strong>BHD</strong><br />

content is 20 vol%. Looking at the cetane index, isomerized <strong>BHD</strong>-blended diesel has a lower cetane<br />

index than normal <strong>BHD</strong>-blended diesel in the case <strong>of</strong> the 10 vol% blend. However, the blend<br />

containing 20 vol% isomerized <strong>BHD</strong> had a cetane index the same as that <strong>of</strong> the 10 vol% normal<br />

<strong>BHD</strong> blend. We found that a diesel oil which contains 20 vol% <strong>of</strong> isomerized <strong>BHD</strong> (isomerization<br />

ratio: 50%) would have properties as good or better than those <strong>of</strong> conventional diesel oil.<br />

Table 7<br />

Properties <strong>of</strong> Isomerized <strong>BHD</strong>-Blended <strong>Diesel</strong> Oil<br />

Normal <strong>BHD</strong> 50% Isomerized <strong>BHD</strong> Conventional<br />

<strong>BHD</strong> Content 10vol% 10vol% 20vol% <strong>Diesel</strong> Fuel<br />

Density g/cm3 0.8103 0.8198 0.8140 0.8283<br />

Viscosity mm2/s 2.828 3.330 3.250 3.254<br />

Distillation T90 ℃ 326.0 330.0 324.5 337.5<br />

CFPP ℃ -10 -14 -12 -9<br />

Cetane index 62.0 58.2 61.3 58.1<br />

4. CONSIDERATION<br />

Through the reaction experiments involving <strong>BHD</strong> isomerization, we were able to obtain<br />

isomerized <strong>BHD</strong>, and showed that the isomerization ratio can be controlled over a wide range<br />

through careful selection <strong>of</strong> the catalysts and reaction conditions. In <strong>BHD</strong> isomerization, the cracking<br />

reaction occurs as a sub reaction. It is important to select a catalyst system and reaction conditions that<br />

minimize cracking, while staying <strong>with</strong>in a range in which the isomerization ratio is sufficient.<br />

Isomerization improved the cold flow properties <strong>of</strong> <strong>BHD</strong>, and expanded the range <strong>of</strong> usable <strong>BHD</strong><br />

blend ratios. One <strong>of</strong> the advantages <strong>of</strong> <strong>BHD</strong> is a high cetane number. Isomerization does not cause a<br />

major decline in cetane number, meaning that isomerized <strong>BHD</strong> still has the same advantage.<br />

Palm oil and other vegetable oils (rapeseed, sunflower, soybean, corn, etc.) are used as cooking<br />

oils all over the world. If these oils are to be used for automotive fuels, it will probably not happen by<br />

getting people to use less for cooking. And if we simply increase cultivation, there is a risk <strong>of</strong> serious<br />

environmental destruction. We need to thoroughly consider how sources <strong>of</strong> raw materials can be

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