Method for regeneration of used lubricating oils
A method for the regeneration of used lubricating oils to produce lubricant base oils includes the steps of (a) removing resin and impurities by distillation, (b) catalytic oxidation treatment and (c) adsorption process. The method can efficiently reduce the color, metal ions, and sulfur content under mild reaction conditions at low cost and obtain high yield of regenerated oil above 85 wt. %.
1. A method for regenerating a used lubricating oil, comprising:
subjecting the used lubricating oil to vacuum distillation to obtain a lube base oil;
adding the lube base oil, water, an oxidizing agent, and a catalyst in a reactor, wherein the lube base oil is catalytically oxidized to form a reaction mixture containing an oxidized oil product;
separating the oxidized oil from the reaction mixture; and
passing the oxidized oil through an adsorption column to obtain a purified lubricating oil.
2. The method according to claim 1 , wherein the catalytic oxidation and the adsorption step are carried out at a temperature of 0-100° C.
3. The method according to claim 1 , wherein the oxidizing agent is a gas oxidizing agent, a liquid oxidizing agent, or a combination thereof.
4. The method according to claim 1 , wherein the used lubricating oil is used engine lube oil, used gear lube oil, used hydraulic oil, used turbine oil, used heating oil, used mineral oil, or waste biomass oil.
5. The method according to claim 2 , wherein the oxidizing agent is oxygen, ozone, or hydrogen peroxide.
6. The method according to claim 1 , wherein the catalyst is a supported multifunctional catalyst comprising one or more transition metals selected from molybdenum, tungsten, cobalt, nickel, iron, and zinc and a support selected from inorganic oxides and molecule sieve/zeolite materials.
7. The method according to claim 1 , wherein the lube base oil is catalytically oxidized for 0.5 to 24 h.
8. The method according to claim 1 , wherein the adsorption column contains a packed adsorbent that is Al 2 O 3 , SiO 2 , or aluminosilicate.
9. The method according to claim 1 , wherein a residence time of the oxidized oil in the adsorption column is 0.5 to 2 h.
10. The method according to claim 2 , wherein the catalytic oxidation and the adsorption step are carried out at ambient temperature.
11. The method according to claim 1 , wherein the oxidized oil is separated from the reaction mixture by centrifiguration.
12. The method according to claim 1 , wherein the oxidizing agent is oxygen.
13. The method according to claim 2 , wherein the oxidizing agent is ozone.
14. The method according to claim 1 , wherein a volume ratio of the lube base oil and the added water is 1:5.