US2009005275A1PendingUtilityA1
Power steering fluid
Est. expiryJun 28, 2027(~1 yrs left)· nominal 20-yr term from priority
C10N 2030/74C10N 2040/04C10M 171/02C10N 2030/02C10N 2030/08C10M 2205/173C10N 2020/02C10N 2040/08C10N 2070/00
43
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Claims
Abstract
Provided are power steering fluids made from a waxy feed and with improved low temperature properties, such as, for example, a viscosity index of greater than 290 and a Brookfield Viscosity at −40° C. of less than 1900 mPa·s. In an embodiment, the power steering fluid comprises greater than 50 weight % base oil, viscosity index improver, and less than about 1.0 weight % pour point depressant.
Claims
exact text as granted — not AI-modified1 . A power steering fluid comprising:
a) greater than 50 weight % base oil, wherein the base oil has consecutive numbers of carbon atoms and has a viscosity index greater than a Viscosity Index Factor calculated by the following equation:
28×ln(Kinematic Viscosity at 100° C.)+101; and
b) viscosity index improver; wherein the power steering fluid has a viscosity index of greater than 290 and a Brookfield Viscosity at −40° C. of less than 1900 mPa·s.
2 . The power steering fluid of claim 1 , further comprising less than about 1.0 weight % pour point depressant.
3 . The power steering fluid of claim 1 , wherein the base oil is made from a waxy feed.
4 . The power steering fluid of claim 1 , wherein the base oil has a kinematic viscosity at 100° C. between about 1.2 and about 4.0 mm 2 /s.
5 . The power steering fluid of claim 1 , wherein the base oil has a kinematic viscosity at 100° C. between about 1.5 and about 3.5 mm 2 /s.
6 . The power steering fluid of claim 1 , wherein the base oil has greater than 5.0 weight % molecules with cycloparaffinic functionality.
7 . The power steering fluid of claim 1 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 5.
8 . The power steering fluid of claim 1 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 10.
9 . The power steering fluid of claim 1 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 15.
10 . The power steering fluid of claim 1 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 20.
11 . The power steering fluid of claim 1 , comprising greater than 70 weight % base oil.
12 . The power steering fluid of claim 1 , comprising viscosity index improver in an amount less than 13 weight %.
13 . The power steering fluid of claim 1 , comprising viscosity index improver in an amount less than 12 weight %.
14 . The power steering fluid of claim 1 , wherein the power steering fluid comprises approximately 0 weight % pour point depressant.
15 . The power steering fluid of claim 1 , wherein the Brookfield Viscosity at −40° C. is less than 1500 mPa·s.
16 . The power steering fluid of claim 1 , further comprising a detergent-inhibitor additive package.
17 . The power steering fluid of claim 16 , comprising 2 to 6 weight % detergent-inhibitor additive package.
18 . The power steering fluid of claim 16 , comprising less than 5 weight % detergent-inhibitor additive package.
19 . The power steering fluid of claim 1 , wherein the base oil is Fischer-Tropsch derived.
20 . The power steering fluid of claim 1 , wherein the power steering fluid meets the requirements of one or more power steering fluid specifications for automotive power steering systems.
21 . A process for producing the power steering fluid of claim 1 comprising:
a) obtaining a base oil having:
i) a consecutive numbers of carbon atoms;
ii) a viscosity index greater than a Viscosity Index Factor calculated by the following equation:
28×ln(Kinematic Viscosity at 100° C.)+101; and
b) blending the base oil with viscosity index improver to form the power steering fluid; wherein the power steering fluid comprises greater than 50 weight % base oil and has a viscosity index of greater than 290 and a Brookfield Viscosity at −40° C. of less than 1900 mPa·s.
22 . A process for producing a power steering fluid comprising:
a) obtaining a base oil having:
i) a consecutive numbers of carbon atoms;
ii) a kinematic viscosity at 100° C. of less than about 4 mm 2 /s; and
iii) a Noack volatility less than a Noack Volatility Factor calculated by the following equation:
160−40(Kinematic Viscosity at 100° C.); and
b) blending the base oil with viscosity index improver to form the power steering fluid; wherein the power steering fluid comprises greater than 50 weight % base oil and has a viscosity index of greater than 290 and a Brookfield Viscosity at −40° C. of less than 1900 mPa·s.
23 . The process of claim 22 , wherein forming a power steering fluid further comprises blending the base oil with pour point depressant, wherein the power steering fluid comprises less than about 1.0 weight % pour point depressant.
24 . The process of claim 22 , wherein the base oil has a viscosity index greater than a Viscosity Index Factor calculated by the following equation:
28×ln(Kinematic Viscosity at 100° C.)+101.
25 . The process of claim 22 , wherein the base oil has a kinematic viscosity at 100° C. between about 1.2 and about 4.0 mm 2 /s.
26 . The process of claim 22 , wherein the base oil has a kinematic viscosity at 100° C. between about 1.5 and about 3.5 mm 2 /s.
27 . The process of claim 22 , wherein the base oil is Fischer-Tropsch derived.
28 . The process of claim 22 , wherein the base oil has greater than 5.0 weight % molecules with cycloparaffinic functionality.
29 . The process of claim 22 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 5.
30 . The process of claim 22 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 10.
31 . The process of claim 22 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 15.
32 . The process of claim 22 , wherein the base oil has a ratio of molecules with monocycloparaffinic functionality to molecules with multicycloparaffinic functionality of greater than 20.
33 . The process of claim 22 , wherein forming a power steering fluid further comprises blending the base oil with a detergent-inhibitor additive package.
34 . The process of claim 33 , wherein the detergent-inhibitor additive package is blended in an amount of 2 to 6 weight %.
35 . The process of claim 33 , wherein the detergent-inhibitor additive package is blended in an amount of less than 5 weight %.
36 . The process of claim 22 , wherein the base oil has an aniline point greater than
36×ln(Kinematic Viscosity at 100° C.)+200.
37 . The process of claim 22 , wherein the base oil has a Noack volatility between 0 and 100.
38 . The process of claim 37 , wherein the base oil has a Noack volatility less than a Noack Volatility Factor calculated by the following equation:
900×(Kinematic Viscosity at 100° C.) −2.8 −15.
39 . A power steering fluid produced by the process of claim 22 comprising:
a) greater than 50 weight % base oil, wherein the base oil has consecutive numbers of carbon atoms, a kinematic viscosity at 100° C. of less than about 4 mm 2 /s, and a Noack volatility less than a Noack Volatility Factor calculated by the following equation:
160−40(Kinematic Viscosity at 100° C.); and
b) viscosity index improver; wherein the power steering fluid has a viscosity index of greater than 290 and a Brookfield Viscosity at −40° C. of less than 1900 mPa·s.Cited by (0)
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