IP Library Granted Patent US 8,927,470
Granted Patent B2
US 8,927,470 · App. 12/302,342 · Granted Jan 6, 2015

Process and apparatus for preparing a soap concentrate, a lubricating composition, and combinations thereof

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Quick Facts
Patent No.
US 8,927,470
App. No.
12/302,342
Granted
Jan 6, 2015
Kind
B2
Abstract

The invention provides for a process and apparatus for preparing a soap concentrate, including: (a) introducing feed components to a first feeding zone; (b) first reacting in a first reacting zone; (c) first venting in a first venting zone; and (d) cooling in a cooling zone. The process may further include, after (c) and before (d): (i) continued reacting in a continued reacting zone; and (ii) second venting in a second venting zone. The invention also provides for a process and apparatus for preparing a lubricating composition comprising: (aa) introducing a soap concentrate and a base oil to a lubricating composition feeding zone; (bb) dispersing the soap concentrate in a lubricating composition dispersing zone; (cc) mixing the soap concentrate and the base oil in a lubricating composition mixing zone; and (dd) cooling in a lubricating composition cooling zone.

Claims (32)

1. A process for preparing a soap concentrate comprising:

providing an apparatus comprising an extruder and a plurality of zones arranged in series and in fluid communication, wherein the plurality of zones comprise (a) a first feeding zone; (b) a first reacting zone; (c) a first venting zone; and (d) a cooling zone, and wherein the zones are in the order (a), (b), (c), (d);

introducing feed components to the first feeding zone (a);

allowing the feed components to react in the first reacting zone (b);

allowing venting from the first venting zone (c);

allowing output to be cooled within the cooling zone (d); and

thereby obtaining the soap concentrate.

2. A process according to claim 1 wherein the apparatus further comprises a continued reacting zone and a second venting zone and further comprising, after (c) and before (d), (i) allowing continued reacting in the continued reacting zone; and (ii) allowing second venting in the second venting zone.

3. A process according to claim 1 wherein the apparatus further comprises a second feeding zone and further comprising introducing one or more initial additives to the second feeding zone.

4. A process according to claim 1 wherein the apparatus further comprises a water injecting zone and further comprising injecting water in the water injecting zone.

5. A process according to claim 1 wherein the soap concentrate comprises at least one concentrate selected from the group consisting of lithium soap concentrate, lithium complex soap concentrate, lithium-calcium soap concentrate, and calcium complex soap concentrate.

6. A process according to claim 1 further comprising combining the soap concentrate with a base oil to prepare a base grease.

7. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil in an amount of 75 weight percent to 95 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, and a combination thereof in an amount of 8 weight percent to 20 weight percent, based on the total weight of the soap concentrate.

8. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil in an amount of 75 weight percent to 95 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, calcium hydroxide, and a combination thereof in an amount of 8 weight percent to 20 weight percent, based on the total weight of the soap concentrate.

9. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil fatty acid in an amount of 75 weight percent to 95 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, and a combination thereof in an amount of 8 weight percent to 20 weight percent, based on the total weight of the soap concentrate.

10. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil fatty acid in an amount of 75 weight percent to 95 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, calcium hydroxide, and a combination thereof in an amount of 8 weight percent to 20 weight percent, based on the total weight of the soap concentrate.

11. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil or hydrogenated castor oil fatty acid in an amount of 50 weight percent to 65 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, and a combination thereof in an amount of 10 weight percent to 20 weight percent, based on the total weight of the soap concentrate; and

a complexing agent in an amount of 6 weight percent to 12 weight percent, based on the total weight of the soap concentrate.

12. A process according to claim 1 wherein the feed components comprise:

hydrogenated castor oil or hydrogenated castor oil fatty acid in an amount of 50 weight percent to 65 weight percent, based on the total weight of the soap concentrate; and

at least one selected from the group consisting of lithium hydroxide, lithium hydroxide monohydrate, calcium hydroxide and a combination thereof in an amount of 10 weight percent to 20 weight percent, based on the total weight of the soap concentrate; and

a complexing agent in an amount of 6 weight percent to 12 weight percent, based on the total weight of the soap concentrate.

Assignments (3)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 14, 2010
From: BROSSAUD, JEAN-LUC PIERRE ANDRE; CODE, DAVID EDMUND; DABOS, JEROME; HOLLEY, JEAN-CLAUDE EMILE MAXIMILIEN; HUANG, AIMIN; KAUSHIK, KRISHNA RANGRAJ; MAILLARD, CATHERINE; MENON, RAGHUNATH GOPAL; SAINT, JEAN-PAUL; SCHADE, RAINER HANS
To: SHELL OIL COMPANY
Reel/Frame 023780/0667 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 6, 2009
From: ROSSAUD, JEAN-LUC PIERRE ANDRE; CODE, DAVID EDMUND; DABOS, JEROME; HOLLEY, JEAN-CLAUDE EMILE MAXIMILIEN; HUANG, AIMIN; KAUSHIK, KRISHNA RANGRAJ; MAILLARD, CATHERINE; MENON, RAGHUNATH GOPAL; SAINT, JEAN-PAUL; SCHADE, RAINER HANS
To: SHELL OIL COMPANY
Reel/Frame 022357/0001 →