Continuous process for the manufacture of grease

Patent metadata

Field	Value
Publication number	US-2019016984-A1
Application number	US-201816029873-A
Country	US
Kind code	A1
Filing date	Jul 9, 2018
Priority date	Jul 13, 2017
Publication date	Jan 17, 2019
Grant date	—

Abstract

This disclosure relates to a continuous process for preparing a grease thickener product in which operating conditions of the continuous process can be varied to obtain desired grease product properties. The process includes: (a) introducing a C 3 to C 30 hydroxy fatty acid or a C 3 to C 30 hydroxy fatty acid ester, and a metal base into a reaction zone; (b) operating the reaction zone at a temperature between 100° C. and 240° C. to react the C 3 to C 30 hydroxy fatty acid or the C 3 to C 30 hydroxy fatty acid ester, and the metal base, to produce a grease thickener product; (c) introducing the grease thickener product of step (b) into a flash chamber zone; and (d) operating the flash chamber zone at a temperature sufficient to remove volatiles from the grease thickener product of step (b). The continuous process conditions afford a production throughput of grease thickener product of greater than 8,000 pounds per hour.

First claim

1 . A continuous process for preparing a grease thickener product, said process comprising:
(a) introducing a C 3 to C 30 hydroxy fatty acid or a C 3 to C 30 hydroxy fatty acid ester, and a metal base into a reaction zone; (b) operating the reaction zone at a temperature between about 100° C. and about 240° C. to react the C 3 to C 30 hydroxy fatty acid or the C 3 to C 30 hydroxy fatty acid ester, and the metal base, to produce a grease thickener product; (c) introducing the grease thickener product of step (b) into a flash chamber zone; and (d) operating the flash chamber zone at a temperature sufficient to remove volatiles from the grease thickener product of step (b);
wherein continuous process conditions afford a production throughput of grease thickener product of greater than about 8,000 pounds per hour.

2 . The continuous process of claim 1 , further comprising:
(e) passing the grease thickener product of step (b) through a reaction zone back pressure valve operated between about 10 and about 300 psig; (f) passing the grease thickener product of step (e) through a heat exchanger operated at a temperature between about 100° C. and 240° C.; (g) passing the grease thickener product of step (f) through a heat exchanger back pressure valve operated between about 10 and about 300 psig; and (h) passing the grease thickener product of step (d) through a finishing or shear valve operated between about 10 and about 300 psig.

3 . The continuous process of claim 1 further comprising:
(i) removing and recycling at least a portion of the grease thickener product of step (b) back through the reaction zone; and
(j) passing the grease thickener product of step (i) through a reaction zone recycle pump that is sized to achieve a recycle rate from about 0.5 to about 20 pounds per minute.

4 . The continuous process of claim 1 further comprising:
(k) removing and recycling at least a portion of the grease thickener product of step (d) back through the flash chamber zone; and
(l) passing the grease thickener product of step (k) through a flash chamber zone recycle pump that is sized to achieve a recycle rate from about 0.5 to about 20 pounds per minute, and a flash chamber zone recycle valve operated between about 10 and about 300 psig.

5 . The continuous process of claim 1 further comprising:
(m)introducing one or more base oils into the reaction zone;
(n) operating the reaction zone at a temperature between about 100° C. and about 240° C. to react the C 3 to C 30 hydroxy fatty acid or the C 3 to C 30 hydroxy fatty acid ester, and the metal base, in the presence of the one or more base oils, to produce a grease reaction product.

6 . The continuous process of claim 1 further comprising:
(o) introducing one or more grease additives into the grease thickener product of step (d), said one or more grease additives comprising borated esters, polymers, antiwear agents, extreme pressure agents, rust and corrosion inhibitors, boundary lubrication additives, metal passivators, antioxidants, antifoam and defoamants, dispersants, detergents, free radical scavengers, chelating agents, and/or ionic liquids.

7 . The continuous process of claim 5 further comprising:
(p) introducing one or more grease additives into the one or more base oils, said one or more grease additives comprising reactive polymers, defoamants, antiwear agents, extreme pressure agents, rust and corrosion inhibitors, boundary lubrication additives, metal passivators, antioxidants, antifoam agents, dispersants, detergents, free radical scavengers, chelating agents, and/or ionic liquids.

8 . The continuous process of claim 1 further comprising:
(q) introducing a complexing agent into the grease thickener product of step (e) or step (f).

9 . The continuous process of claim 1 wherein the C 3 to C 30 hydroxy fatty acid is 12-hydroxy stearic acid.

10 . The continuous process of claim 1 wherein the C 3 to C 30 hydroxy fatty acid ester is the methyl or ethyl ester of 12-hydroxy stearic acid.

11 . The continuous process of claim 1 wherein the metal base is lithium oxide, lithium hydroxide, lithium hydroxide monohydrate, or lithium carbonate.

12 . The continuous process of claim 5 wherein the one or more base oils comprise a Group I, Group II, Group III, Group IV, Group V base oil, and combinations thereof.

13 . The continuous process of claim 8 wherein the complexing agent comprises substituted or unsubstituted dibasic acids, boric acid, methyl salicylate, borated additives, and mixtures thereof.

14 . The continuous process of claim 1 wherein continuous process conditions afford a production throughput of grease thickener product of greater than about 10,000 pounds per hour.

15 . The continuous process of claim 1 wherein continuous process conditions afford a production throughput of grease thickener product of greater than about 12,000 pounds per hour.

16 . A continuous process for preparing a grease reaction product, said process comprising:
(a) passing one or more base oils through a heat exchanger operated at a temperature between about 100° C. and 240° C.; (b) introducing the one or more base oils of step (a), a C 3 to C 30 hydroxy fatty acid or a C 3 to C 30 hydroxy fatty acid ester, and a metal base into a reaction zone; (c) operating the reaction zone at a temperature between about 100° C. and about 240° C. to react the C 3 to C 30 hydroxy fatty acid or the C 3 to C 30 hydroxy fatty acid ester, and the metal base, in the presence of the one or more base oils, to produce a grease reaction product; (d) introducing the grease reaction product of step (c) into a flash chamber zone; and (e) operating the flash chamber zone at a temperature sufficient to remove volatiles from the grease reaction product of step (c); wherein continuous process conditions afford a production throughput of grease reaction product of greater than about 8,000 pounds per hour.

17 . The continuous process of claim 16 , further comprising:
(f) passing the grease reaction product of step (c) through a reaction zone back pressure valve operated between about 10 and about 300 psig; (g) passing the grease reaction product of step (f) through a heat exchanger operated at a temperature between about 100° C. and 240° C.; (h) passing the grease reaction product of step (g) through a heat exchanger back pressure valve operated between about 10 and about 300 psig; and (i) passing the grease reaction product of step (e) through a finishing or shear valve operated between about 10 and about 300 psig.

18 . The continuous process of claim 16 further comprising:
(j) removing and recycling at least a portion of the grease reaction product of step (c) back through the reaction zone; and
(k) passing the grease reaction product of step (j) through a reaction zone recycle pump that is sized to achieve a recycle rate from about 0.5 to about 20 pounds per minute.

19 . The continuous process of claim 16 further comprising:
(l) removing and recycling at least a portion of the grease reaction product of step (e) back through the flash chamber zone; and
(m)passing the grease reaction product of step (l) through a flash chamber zone recycle pump that is sized to achieve a recycle rate from about 0.5 to about 20 pounds per minute, and a flash chamber zone recycle valve operated between about 10 and about 300 psig.

20 . The continuous process of claim 16 further comprising:
(n) introducing one or more grease additives into t

Assignees

• Exxonmobil Res & Eng Co

Inventors

• Emett Craig J
• Graham John K
• Zacharkow John
• BRABEZ Nabila
• Spagnoli James E

Classifications

• C10M2207/1276

  used as thickening agent · CPC title

• C10M2203/1006

  used as base material · CPC title

• C10M2207/1285

  used as thickening agents · 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

• C10M2207/1446

  used as thickening agent · CPC title