Method of making a grease thickener and the thickener made by the method

Patent metadata

Field	Value
Publication number	US-11359157-B2
Application number	US-201916972237-A
Country	US
Kind code	B2
Filing date	Jun 27, 2019
Priority date	Jun 28, 2018
Publication date	Jun 14, 2022
Grant date	Jun 14, 2022

Abstract

A continuous process for producing a polyurea concentrate or powder. The process includes combing at least one amine and an isocyanate in the presence of a liquid diluent or a base oil in a rotor stator mixer. The concentrate comprises a polyurea in a base oil wherein the concentration of from about 20 weight percent to about 50, or 40 or 35 or 30 weight percent of polyurea based on total weight of grease thickener. The powder has particle size of 2 to 400 microns. This concentrate or powder can then be formulated by grease manufacturers to the desired final properties without the need for handling of the isocyanate and amine raw materials.

First claim

What is claimed is:

1. A process comprising feeding at least one amine and a first base oil to a front end of a rotor stator mixer which is operating at a shear rate of less than 5000 reciprocal seconds (1/sec), adding an isocyanate to the mixer in a shear zone of the rotor stator mixer and in a position located at a distance from an outlet of the rotor stator mixer that is no more than half the diameter of the rotor stator mixer such that a residence time in the mixer after addition of the isocyanate is less than 20 seconds to produce a grease thickener concentrate comprising a polyurea.

2. The process of claim 1 characterized in that the process is continuous.

3. The process of claim 1 wherein the at least one amine is a mixture
comprising a first linear primary amines having six to eighteen carbon atoms and either a second linear primary amines having six to eighteen carbon atoms and being different from the first linear primary amine or a cyclic primary amine.

4. The process of claim 1 wherein the residence time is less than 10 seconds.

5. The process of claim 1 wherein the residence time is less than 5 seconds.

6. The process of claim 1 wherein the at least one amine is a primary amine and the isocyanate is a di-isocyanate such that the polyurea formed is a diurea.

7. The process of claim 1 wherein the at least one amine comprises an alkylamine and a fatty amine.

8. The process of claim 1 wherein the grease thickener concentrate comprises at least 20 weight percent of the polyurea based on total weight of the grease thickener concentrate.

9. The process of claim 1 wherein the first base oil is selected from API Groups I, II, III, IV or V.

10. The process of claim 1 further comprising diluting the grease thickener concentrate with a second base oil and adding an additive selected from antioxidants; antiwear compounds; extreme pressure compounds, rust and corrosion inhibitors; tackifiers; detergents; dispersants; antifoaming additives; and combinations thereof to form a grease.

11. The process of claim 10 wherein the second base oil is the same as the first base oil.

12. A process comprising reacting an amine and a polyisocyanate in the presence of a liquid diluent in a rotor stator mixer under conditions sufficient to produce a dispersion of a polyurea compound in the liquid diluent wherein the amine is fed to the rotor stator mixer at a front end of the mixer and the polyisocyanate is fed to the rotor stator mixer at a distance that is no more than half the diameter of the rotor stator mixer from an outlet of the rotor stator mixer and directly into a shear zone of the rotor stator mixer to form a polyurea.

13. The process of claim 12 further comprising recovering the polyurea in a dry,
solid particulate form having average particle size of 2 to 400 microns.

14. The process of claim 13 further comprising mixing a base lubricating oil and the dry solid particulate form of the polyurea to form a mixture; heating the mixture to a temperature in the range of from 150° C. to 180° C.; and thereafter milling the heated mixture to form a homogenized grease.

Assignees

• Dow Global Technologies Llc

Inventors

• Jia Zhe
• Cuthbert John B
• Malotky David L
• Saba Stacey A
• Hook Bruce D
• Wilmot Nathan
• Dermody Daniel L

Classifications

• C10M119/24 Primary

  containing nitrogen · CPC title

• C10M2203/003

  used as base material · CPC title

• C10M2215/24

  having hydrocarbon substituents containing thirty or more carbon atoms, e.g. nitrogen derivatives of substituted succinic acid · CPC title

• C10N2030/68

  Shear stability · CPC title

• C10M177/00

  Special methods of preparation of lubricating compositions; Chemical modification by after-treatment of components or of the whole of a lubricating composition, not covered by other classes · CPC title