Membrane separation of used oil and compositions generated

Patent metadata

Field	Value
Publication number	US-12540290-B2
Application number	US-202117919195-A
Country	US
Kind code	B2
Filing date	Mar 17, 2021
Priority date	Apr 20, 2020
Publication date	Feb 3, 2026
Grant date	Feb 3, 2026

Abstract

In an embodiment is provided a process to re-refine used oil that includes introducing a used oil and a solvent to a separation unit under separation conditions selected to produce a purified oil product, the separation unit comprising a porous membrane, a semiporous membrane, or both; and separating the used oil to obtain an effluent comprising a purified oil product. In another embodiment is provided an apparatus for re-refining used oil that includes a separation unit comprising a porous or semiporous membrane; a used oil feed coupled to an inlet of the separation unit; and an inlet of a diffusate collection unit coupled to an outlet of the separation unit. In another embodiment is provided a composition generated from a membrane separation process that includes a base oil, the composition having a soot content of about 0.05% or less.

First claim

What is claimed is:

1 . A process to re-refine used oil, comprising:
introducing a used oil comprising soot content and metal content, and a solvent to a separation unit under separation conditions selected to produce a purified oil product, wherein the separation unit comprises a porous membrane, a semiporous membrane, or both; and separating, via the separation unit, the used oil to obtain a diffusate and a retentate, the diffusate comprising the purified oil product and a portion of the soot content making up 0.09% or less of the diffusate, and the retentate comprising a remaining portion of the soot content not in the diffusate and at least 90% of the metal content, wherein the metal content of the retentate isolates the remaining portion of the soot content not in the diffusate away from the diffusate, wherein the porous membrane or semiporous membrane has a molecular weight cut-off of 2,000 Daltons or less, and wherein the solvent is selected from the group consisting of pentane, hexane, heptane, benzene, toluene, xylene, methanol, ethanol, 1-propanol, methyl ethyl ketone, methyl isobutyl ketone, and combinations thereof.

2 . The process of claim 1 , further comprising removing the solvent by distillation, extraction, fractionation, decanting, or a combination thereof.

3 . The process of claim 1 , wherein the separation conditions comprise a residence time of the used oil in the separation unit, wherein the residence time is 72 hours or less.

4 . The process of claim 1 , wherein the separation conditions comprise an operating temperature of from about 15° C. to about 150° C.

5 . The process of claim 1 , wherein the used oil is a used crankcase oil, used engine oil, used hydraulic oil, used transformer oil, used refrigerator oil, used white oil, used compressor oil, used gas engine oils, used marine engine oils, or a combination thereof.

6 . The process of claim 1 , wherein the porous membrane or semiporous membrane is a latex containing material, a polyamide containing material, a cellulose containing material, a polycarbonate containing material, a polysulfone containing material, or a combination thereof.

7 . The process of claim 1 , wherein the portion of the soot content makes up 0.05% or less of the diffusate as determined by ASTM D5967-A4.

8 . The process of claim 1 , wherein the diffusate comprises a portion of the metal content comprising an amount of Zn, Mg, Ca, Mo, Fe, or a combination thereof of 100 ppm or less as determined by ASTM 5185.

9 . The process of claim 1 further comprising removing water from the used oil prior to introducing the used oil to the separation unit.

10 . The process of claim 1 further comprising removing the solvent from the diffusate, the retentate, or both.

11 . The process of claim 1 further comprising:
hydrotreating the diffusate comprising the purified oil product;
separating the purified oil product into one or more base oil fractions; or
a combination thereof.

12 . The process of claim 1 , wherein the separation conditions comprise a residence time of the used oil in the separation unit, wherein the residence time is from about 16 hours to about 48 hours.

13 . The process of claim 1 , wherein the separation conditions comprise an operating temperature of from about 15° C. to about 60° C.

14 . The process of claim 1 , wherein the separation conditions comprise an operating temperature of from about 15° C. to about 30° C.

15 . The method of claim 1 wherein the purified oil product comprises the portion of the soot content, the portion of the soot content making up 0.01% to about 2% as determined by ASTM D5967-A4.

16 . The method of claim 1 wherein at least a portion of the metal content is from an oil additive comprising at least one additive selected from the group consisting of a dispersant, a detergent, a corrosion inhibitor, a rust inhibitor, a metal deactivator, an anti-wear agent, an extreme pressure additives, an anti-seizure agent, a wax modifier, a viscosity index improver, a viscosity modifier, a fluid-loss additive, a seal compatibility agent, a friction modifier, a lubricity agent, an anti-staining agent, a chromophoric agent, a defoamant, a demulsifier, an emulsifier, a densifier, a wetting agent, a gelling agent, a tackiness agent, a colorant, and a combinations thereof.

Assignees

• Exxonmobil Technology & Engineering Company

Inventors

• Zielinski Christine A
• Naegely Paul C
• Shah Meha H
• Baker Jr Charles L
• Wang Chengrong

Classifications

• B01D2311/25

  Recirculation, recycling or bypass, e.g. recirculation of concentrate into the feed · CPC title

• C10M175/005

  using extraction processes; apparatus therefor · CPC title

• C10M175/0033

  using distillation processes; devices therefor · CPC title

• C10M175/0041 Primary

  by hydrogenation processes · CPC title

• B01D2311/2523

  to feed side · CPC title