Grease composition
US-9404061-B2 · Aug 2, 2016 · US
US2020362258A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020362258-A1 |
| Application number | US-202016945322-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 31, 2020 |
| Priority date | Dec 28, 2016 |
| Publication date | Nov 19, 2020 |
| Grant date | — |
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Compounds having the formula (F-I) below are provided herein: wherein R 1 and R 2 at each occurrence are independently a C 1 -C 5000 alkyl group; R 3 at each occurrence is independently hydrogen or a C 1 -C 5000 alkyl group; R 4 is a C 1 -C 50 alkyl group or an unsubstituted or substituted phenyl group; R 5 at each occurrence is independently hydrogen or a C 1 -C 30 alkyl group; n is 1, 2, 3, or 4; and m+n is 5. Processes for preparing compounds of formula (F-I) as well as base stock and lubricant compositions containing compounds of formula (F-I) are also provided.
Opening claim text (preview).
1 - 14 . (canceled) 15 . A process for making a compound of claim 1 comprising: reacting a compound having the following formula (F-Ia): with an olefin-containing material comprising a compound having the following formula (F-Ib): in the presence of an acid catalyst. 16 . The process of claim 15 , wherein the olefin-containing material comprises at least about 75 wt % of the compound of formula (F-Ib) where R 3 is hydrogen. 17 . The process of claim 15 , wherein the olefin-containing material comprises at least about 50 wt % of the compound of formula (F-Ib) where R 3 is a C 1 -C 100 alkyl group. 18 . The process of claim 15 , wherein the olefin-containing material comprises a mixture of: (i) about 1.0 to about 99 wt % of the compound of formula (F-Ib) where R 3 is hydrogen; and (ii) about 1.0 to about 99 wt % of the compound of formula (F-Ib) where R 3 is a C 1 -C 100 alkyl group. 19 . The process of claim 15 , wherein the olefin-containing material has an isotacticity of at least about 60 mol %. 20 . The process of claim 15 , wherein the acid catalyst is a solid acid catalyst selected from the group consisting of a solid Lewis acid, an acid clay, a polymeric acidic resin, silica-alumina, a mineral acid and a combination thereof. 21 . The process of claim 15 , wherein the acid catalyst comprises one or more molecular sieve having a framework structure selected from the group consisting of BEA, EUO, FAU, FER, HEU, MEL, MFI, MOR, MRE, MTW, MTT, MWW, OFF, and combinations thereof. 22 . The process of claim 21 , wherein the molecular sieve is selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-48, ZSM-50, Zeolite Beta, MCM-56, MCM-22, MCM-36, MCM-49, zeolite Y, zeolite X, and combinations thereof. 23 . The process of claim 15 , wherein at least about 50 mol % of the compounds produced have the moiety comprising R 1 , R 2 , and R 3 bonded to the phenyl ring at a position para to the —O—R 4 moiety. 24 . A lubricant base stock comprising one or more of the compound of claim 1 , wherein the lubricant base stock has one or more of: (i) a hydrolytic stability, measured according to ASTM D-2619, of about 0.01 to about 1.0 mg KOH/g; (ii) a solubility of measured according to Fedors Correlation, of about 8 to about 10 d(i) at 25° C. (cal/cc) A 1/2; and (iii) a rotating pressure vessel oxidation test (RPVOT) break time, measured according to ASTM D-2272, of at least about 200 minutes. 25 . A formulated lubricant composition comprising one or more of the lubricant base stocks of claim 24 in an amount from about 5 wt % to about 90 wt %, based on the total weight of the formulated lubricant composition.
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