البحـث الأول
مجلة النفط والتعاون العربي
161
العدد
- 2017
أربعون
المجلد الثالث و ال
2016
أوابك العلمية لعام
�
ص لبحوث العلمية الفائزة بجائزة
�
عدد خا
45
35
Chapter 3 - Virgin and Used Oil Processing
Re-refining is defined as the chemical and physical processes that extract the
lubricating base stock from used lubricants where water, fuels, additives remnants
and sludge are separated from the base stock.
But it is perhaps better to consider first the steps to produce virgin base oils before
embarking on the processes of re-refining used lubricants. There are some
similarities between the two manufacturing processes that may be useful for the
overall understanding.
Virgin Base Oil Processing:
1, 2,49,84,85
Base oil is the name given to lubricants grade oils which are produced, in the
modern industry, in a complex sequence of steps in a refinery as shown in Fig
(1). Their boiling ranges between 300 and 565
o
C
1
and are produced normally by
feeding reduced crude oil from the atmospheric distillation unit to a vacuum unit
column to lower the boiling points and obtain distillates side streams. The vacuum
residue bottoms still contain valuable high viscosity oil that cannot be distilled
and have to be recovered by using a propane solvent in a de-asphalting unit (PDA)
where the propane dissolves the oil leaving heavy asphalt cut to be produced. The
oil produced so is de-asphalted oil (DAO) and propane is recovered and recycled.
The vacuum side streams and the DAO contain components that are undesirable
in lube base stocks. Therefore they are sent in turn to an extraction unit, usually
with a furfural solvent where the solvent absorbs the undesirables especially
aromatics and gives a raffinate with an improved viscosity characteristic ready
for the next step. The furfural solvent is recovered and the extract product is
returned to be used as asphalt cutter or blended with fuel oil or as feed to
conversion processes.
To get rid of the wax the lube streams are sent in turn to a dewaxing unit which
separates the wax, to improve the pour point, either by refrigeration and filtration
or by solvent, refrigeration and filtration. The solvent is often a mixture of MEK
and toluene.