Crude vegetable
oils contain a wide variety of materials including fatty acids, glycerides,
phosphatides, sterols, tocopherols, hydrocarbons, pigments (gossypol and
chlorophyll), stearol glucosides, protein fragments and mucilaginous material.
Refinery process is designed to remove undesirable constituents in crude oils
with minimal oil loss. Physical refinery usually refers to a process that
removes FFA in the crude or degummed oil by evaporation rather than being
neutralized in alkaline refining process.
Deodorization is the major section
in the physical refinery process. In the industry, the crude oil is usually
pre-treated before entering deodorizer. The pre-treatment sections include
degumming and bleaching. For seed oil with high FFA content, an alkaline
refining process may be required. Degumming process is designed to remove
phosphatides and mucilaginous material from the oil. Bleaching is the process
to remove color bodies from the crude oil by adsorption onto the bleaching
earth. Lastly, deodorization is designed to remove the relative volatile
odoriferous compounds from the crude oil.
Generally, the crude oil is heated
to about 105 oC before sent to the drier or degasser to remove
moisture and dissolved gas. The dried oil will be mixed with phosphoric acid
before entering a retention vessel. This retention vessel is designed to
provide time for the coagulation of gums to occur. Here is the place where
degumming process occurs and it is accomplished by hydrating the phosphatides and
similar materials to make them insoluble in oil. Then, the oil slurries are
sent to bleacher where bleaching earth is added in to adsorb the color bodies
in the oil. The degummed-bleached oil is sent to a leaf filter to separate the
oil from bleaching earth. Pre-coating is done by circulating oil in pre-coat
tank to the leaf filter. This is to provide better filtration of bleaching
earth as the cake form on the surface of the filter. the filtered oil is sent
to a buffer tank. From buffer tank, the filtered oil is further refined in the
deodorizer.
There are many type of deodorization
plant available in the market including continuous packed column, semi continuous
tray and many others type. Normally deodorization column will be design with
heat recovery whereby the hot oil leaving from the column bottom will be used
to pre-heat the oil feed into the Deodorizer column. Deodorization column
temperature will be depending on type oil. During deodorization, FFA and other
volatile component is vaporized and sucked out by the vacuum. The RBD oil is
further cooled down by heat exchanger before sent to a polishing filter prior
to storage. The vapor phase from deodorizer is sent to scrubber to recover the
FFA and is collected as fatty acid distillate, FAD. Below is the simplified
process flow diagram for a normal physical refinery plant.
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