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(c)
The converter
for the hydrogenation reaction is
designed for attaining any desired selectivity in hydrogenation.
(d) Continuous type of deodorisation equipment is provided
for the highest possible steam economy, reduction of colour
and reduction of odour.
(e) Design and layout of the blending and packing section
in our plants is such that manual labour is reduced to the
minimum.
(f)
Electrolytic cells are designed for low electricity consumption,
thereby increasing efficiency and reducing space requirements.
(g)
Lower stripping steam usage translates to lower motive steam
consumption by the vacuum system.
(h)
Short residence time of the oil at an elevated temperature
in the prestripper column ensures better oil quality.
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