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Catalysis : an Integrated Approach to Homogeneous ...

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32 2 -CATALYTIC PROCESSES IN INDUSTRY<br />

Typical process conditions are:<br />

Temperature: 350420°C<br />

Pressure: 40-100 bar<br />

LHSV: 1-6 h-'<br />

The severity of the processing conditions depends on the feed; for light petro-<br />

leum fractions it will be milder th<strong>an</strong> for heavy residues. Moreover, it is common<br />

practice <strong>to</strong> compensate for deactivation of the catalyst by increasing the tempera-<br />

ture of the reac<strong>to</strong>r. A simplified flow scheme involving a trickle flow reac<strong>to</strong>r is<br />

shown in Fig. 2.5.<br />

Cutulysts<br />

M<br />

watr<br />

I I<br />

high pressure low pressure<br />

furnace reac<strong>to</strong>r sepora t or stripper separa<strong>to</strong>r<br />

Fig. 2.5. Simplified scheme of hydrotreatment involving a trickle flow reac<strong>to</strong>r.<br />

Catalysts are mixed metal sulphides on a carrier. The major examples are<br />

supported mixed phases of CoS <strong>an</strong>d MoS3 of NiS <strong>an</strong>d MoS2 <strong>an</strong>d NiS <strong>an</strong>d WS2.<br />

There is as yet no full agreement on the structure. For the first catalyst the best<br />

description is small MoS2 clusters with CoS units at the edges. Typical dimen-<br />

sions of these clusters are 1 nm <strong>an</strong>d a stacking between 1 <strong>an</strong>d 3.<br />

Environment<br />

From the point of view of cle<strong>an</strong> technology hydrotreatment is gaining increas-<br />

ing interest. A recent example is diesel fuel. Sulphur-containing compounds in<br />

diesel fuel cause serious difficulties in catalytic cle<strong>an</strong>ing of the exhaust gases.<br />

Undoubtedly, in the near future, novel processes will be needed for the deep<br />

desulphurization of diesel.

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