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166

2016

أوابك العلمية لعام

ص لبحوث العلمية الفائزة بجائزة

عدد خا

مجلة النفط والتعاون العربي

161

العدد

- 2017

أربعون

المجلد الثالث و ال

Re-refining of Used Lubricating Oil and its Economic and Environmental Implications

43

4.18 MRD Technology

The technology based on liquid-liquid extraction was developed by Mineralol-

Raffinerie-Dollbergen (MRD) in the mid-1990s. It is claimed to be one of the latest

solvent extraction processes.

4.18.1

Process description

The MRD process consists of the following steps:

Dewatering stage:

Atmospheric distillation is used for separating water and low-boiling fractions

Vacuum distillation and thin film evaporation:

The extract recovery section also consists of a distillation and a stripping column. Pre-

treated oil is vacuum-distillated with production of a gas oil fraction. Then it is sent to a

special extraction column, where base oil fraction is separated from the extract by

specific solvent(N-Methyl Pyrrolidone), which allows quantitative removing of PAH

and preservation of the positive impact of low temperature viscosity behavior of these

groups of oils.

Solvent Recovery:

The humid solvent separated in the stripping columns of the Raffinate and Extract

recovery sections is returned to the solvent drying column, where excess water is

removed. The ‘dry’ solvent is also returned to the solvent tank. From there, the dry

solvent can again be used for extraction purposes in the extraction column.

4.18.2

Process features and drawbacks

The MRD solvent extraction process is considered the latest development for refining

vacuum distillates from used oils. It is claimed that the novel process developed by

MRD completely satisfies the requirements existing for a modern technology for

producing from used oils high-quality base oils, the properties of which in some

respects are even superior to those of the classical solvent raffinates produced from

petroleum.

A plant is operating near Hanover, in Germany. The re-refinery has a capacity allowing

it to process 230,000 MTPY of used oil and oil-containing liquids. 120,000 MTPY thereof

are used as feedstock for the production of 70,000 MTPY of new base oils.