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

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

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Acid Number<br />

(before test)<br />

Acid Number<br />

(after test)<br />

Palm<br />

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

Palm<br />

FAME<br />

Conventional<br />

<strong>Diesel</strong> Oil<br />

mgKOH/g 0.00 0.26 0.00<br />

mgKOH/g 0.03 10.40 0.07<br />

The cold flow properties <strong>of</strong> the <strong>BHD</strong> are shown in Table 5. The cloud point <strong>of</strong> the <strong>BHD</strong> is about<br />

20°C, slightly worse than FAME. Cloud point is the temperature at which wax (paraffin) begins to<br />

separate when and oil is chilled to a low temperature, and it serves as an important indicator <strong>of</strong><br />

practical performance in automotive applications in low temperatures. The cloud point <strong>of</strong> <strong>BHD</strong><br />

(20°C) is much higher than the value prescribed in the JIS (Japan Industrial Standard) standard, and<br />

thus <strong>BHD</strong> cannot be used by itself in winter.<br />

Table 5<br />

<strong>Cold</strong> <strong>Flow</strong> Properties <strong>of</strong> <strong>BHD</strong><br />

Palm<br />

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

Palm<br />

FAME<br />

Conventional<br />

<strong>Diesel</strong> Oil<br />

Cloud Point ℃ 20 15 -6<br />

Pour Point ℃ 20.0 12.5 -30.0<br />

CFPP ℃ 22 11 -9<br />

This poor low-temperature performance is due to the fact that hydrogenated oil is a straight chain<br />

hydrocarbon (normal paraffin). In the field test, the fuel contained only 10% <strong>BHD</strong>, and its cold flow<br />

properties were acceptable. However, the poor cold flow properties <strong>of</strong> <strong>BHD</strong> are an issue when we<br />

increase the <strong>BHD</strong> content or use the <strong>BHD</strong>-blended diesel in very cold areas. In order to improve the<br />

cold flow properties <strong>of</strong> <strong>BHD</strong>, we isomerized <strong>BHD</strong> (normal paraffin) into iso-paraffin, which has<br />

branched chains in its molecular structure. In the next section, we discuss the examinations.<br />

3. ISOMERIZATION OF <strong>BHD</strong><br />

3.1 Isomerization conditions<br />

We conducted reaction experiments involving <strong>BHD</strong> isomerization using our pilot plants. The<br />

feed <strong>BHD</strong> was made using the method described in the second section. Two kinds <strong>of</strong> noble metal<br />

catalysts (amorphous type and zeolite type) were used. Reaction temperature: 300°–340°C; reaction<br />

pressure: 3-10 MPa; LHSV: 1 h -1 .<br />

3.2 Compositions <strong>of</strong> isomerization products<br />

Typical compositions <strong>of</strong> isomerization products are shown in Fig. 5. Feed <strong>BHD</strong> is isomerized into<br />

iso-paraffin and simultaneously cracked into light fractions whose carbon numbers are lower than<br />

C14. This means that the gas oil fraction will decrease as we proceed <strong>with</strong> the isomerization reaction,<br />

which is necessary to improve cold flow properties. Therefore, when we design the process <strong>of</strong> <strong>BHD</strong>

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