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diesel hydrotreaters revamp a way for increasing production

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44th International Petroleum Conference, Bratislava, Slovak Republic, September 21-22, 2009 4<br />

RESULTS AND DISCUSSION<br />

During the per<strong>for</strong>mance test of the HDS-3 unit the product (stable<br />

hydrogenate) properties were as follows:<br />

- Product properties<br />

Sulphur , wt ppm ≤ 5<br />

Density at 15 °C, kg/m 3 840.5-843.6<br />

Polynuclear aromatics , % 4.6-5.8<br />

These data indicate that the increase of the catalyst volume by a factor<br />

of 1.9 (decreasing the LHSV from 1.7 to 0.90h -1 ) allowed the LNB heavy<br />

middle distillate hydrotreater HDS-3 to produce NZSD. The hydrogen<br />

consumption was found to be 28.3 Nm 3 /m 3 oil which was 8% higher than that<br />

recorded be<strong>for</strong>e the reconstruction (26.3 Nm 3 /m 3 oil).<br />

During the per<strong>for</strong>mance test of the HDS-2 unit the product (stable<br />

hydrogenate) properties were as follows:<br />

- Product properties<br />

Sulphur , wt ppm ≤ 5<br />

Density at 15 °C, kg/m 3 844-845<br />

Polynuclear aromatics , % 4.6-5.8<br />

These data indicate that the increase of the catalyst volume by a factor<br />

of 1.7 (decreasing the LHSV from 2.0 to 1.17h -1 ) allowed the LNB heavy<br />

middle distillate hydrotreater HDS-2 to produce NZSD. The hydrogen<br />

consumption was found to be 34.2 Nm 3 /m 3 oil which was 14% higher than that<br />

recorded be<strong>for</strong>e the reconstruction (30.1 Nm 3 /m 3 oil).<br />

Figures 1 and 2 present the deactivation of the catalyst TK-576 Brim in<br />

the LNB HDS-3 and HDS-2 heavy middle distillate <strong>hydrotreaters</strong>. It is evident<br />

from these data that the catalyst in HDS-2 unit has exhibited higher<br />

deactivation rate of 3.4 0 C/month, than HDS-3 catalyst whose deactivation rate<br />

is 3.0 0 C/month. With a start of run temperature (SORT) of 350 0 C and end of<br />

run temperature (EORT) of 390 0 C a cycle length of 13 months is obtained <strong>for</strong><br />

HDS-3. With a start of run temperature (SORT) of 349 0 C and end of run<br />

temperature (EORT) of 390 0 C also a cycle length of 12 months is obtained <strong>for</strong><br />

HDS-2. The replacement of the older heat exchangers in both units not only<br />

improved reliability but also improved the unit energy efficiency. The cost <strong>for</strong><br />

fuel gas was reduced by a factor of two.

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