Cold Cranking Simulator Viscosity Boosting Base Stocks and Lubricating Oil Formulations Containing the Same
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example 1
yl Paraffins as CCSV-Boosting Base Stocks
[0133]
[0134]Pure 1-tetradecene was dimerized in a continuous stirred-tank reactor in the presence of a metallocene catalyst system comprising biscylopentadienyl zirconium (IV) dichloride and methyl aluminoxane (MAO). MAO served as both a scavenger and a co-catalyst in the process. The catalyst system was dissolved in toluene before being charged into the reactor. Residence time was 6 hours at a reaction temperature of about 70° C. The reaction mixture effluent from the reactor was quenched by using a small quantity of water. Filter aid was added thereafter, and the fluid was filtered to remove Zr and / or Al-containing solid particles. Gas chromatography showed a conversion of the C14 LAO higher than 50%, and a selectivity toward dimers higher than 95%. The resultant unsaturated PAO was then flashed to remove the residual monomer. The unsaturated dimer product was then hydrogenated by reacting with hydrogen in the presence of a hydrogenation ca...
example 2
d Catalyzed, Hydrogenated Dimers of C16 and C18 LAOs as CCSV-Boosting Base Stock
[0138]A series of hydrocarbon materials were made from single, pure LAO monomers, using BF3 as the polymerization catalyst ethanol as a promoter, and ethyl actate as terminator with a promoter / terminator ratio of 1, a polymerization temperature of 50° C., in a two-tank continuous stirred tank reactor with a residence time of 2 hours in the first tank and 1 hour in the second tank, substantially in accordance with the method taught in WO2006 / 101585 A1, mutatis mutandis. To the extent the dimers were made by using a conventional, non-metallocene catalyst, they are called conventional PAOs (“cPAO”s). The polymerization mixtures exiting the second tank were flashed to remove residual monomers to obtain unsaturated products comprising about 90 wt % dimers and about 10 wt % trimers. The unsaturated products were then hydrogenated by hydrogen in the presence of a hydrogenation catalyst to obtain substantially s...
example 3
rs as CCSV-Boosting Base Stocks
[0145]A series of linear, synthetic mono-ester base stocks were prepared by the condensation reaction of linear fatty acids (C10-C18 linear carboxylic acids) and linear primary alcohols (C6-C18 linear primary alcohols). Preferably, the ester has 26 carbons and is prepared from palmitic acid (C16) and n-decanol (C10) to make decyl palmitate. Properties of illustrative linear, synthetic mono-ester base stocks (i.e., decyl palmitate, dodecyl palmitate, decyl stearate, and dodecyl stearate) are shown in Table 2 below.
TABLE 2n-C12n-C10n-C12Propertiesn-C10 PalmitatePalmitateStearateStearateKV100 (cSt)3.143.593.644.18KV40 (cSt)SolidSolidSolidolidVI————NV (%)————Pour Point (° C.)>40>40>40>40Appearance atSolidSolidSolidSolid25° C.
[0146]FIG. 3 graphically shows CCSV-boosting efficacies of a series of waxy esters. As can be seen, the base stocks listed in Table 2 above generated a positive D(ccsv) and a negative D(kv), both highly desired for a CCSV-boosting base...
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