Additive package for high temperature synthetic lubricants
a synthetic lubricant and additive technology, applied in the field of additive packages, can solve the problems of lack of commercial lubricants for chain and drive gear operations, lack of high-temperature stability, etc., and achieve the effect of reducing weight loss
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example 1
[0041] A dipentaerythritol hexaisononanoate ester was prepared in a reaction vessel equipped with a mechanical stirrer, thermocouple, thermoregulator, Dean-Stark trap, condenser, nitrogen sparge and vacuum source. The following materials were charged to the reactor:
INGREDIENTAMOUNT gms (moles)Dipentaerythritol1225 g (4.8 m)Isononanoic acid5175 g (32.75 m)
[0042] The reaction mixture was heated to 185°-190° C. with agitation. The water-of-reaction was collected in and removed from the Dean-Stark trap. The temperature was gradually raised over 5-6 hours to about 230° C. with application of vacuum to maintain reflux. This removed the reaction water and returned the acid collected in the trap to the reactor. These conditions were maintained to a point where the hydroxyl number of the reaction mixture was less than 3.0. The bulk of the excess acid was then removed by vacuum distillation together with nitrogen sparge and then residual acidity was removed with alkali.
[0043] The resulting...
example 2
[0044] A dipentaerythritol ester having a viscosity of about 150 cSt at 40° C. can be prepared in a vessel in the same manner as described for the ester in Example 1. In this case, the following materials are charged to the reactor:
INGREDIENTAMOUNT gms (moles)Dipentaerythritol1225 g (4.8 m) Heptanoic acid597 g (4.59 m)Caprylic / capric acid1094 g (7.06 m) Isononanoic acid3283 g (20.78 m)
[0045] The reaction mixture is heated to 185°-190° C. with agitation. The water-of-reaction is collected in and removed from the Dean-Stark trap. The temperature is gradually raised over 5-6 hours to about 230° C. with application of vacuum to maintain reflux. This removes the reaction water and returns the acid collected in the trap to the reactor. These conditions are maintained to a point where the hydroxyl number of the reaction mixture is less than 3.0. The bulk of the excess acid is then removed by vacuum distillation together with nitrogen sparge and then residual acidity was removed with alka...
example 3
[0047] An additive package of an oligomeric amine antioxidant and borated antiwear agent in accordance with the invention was added to the polyol esters prepared in Example 1 to formulate the lubricating fluid. The esters of Runs 1 and 2 from Example 1 were formulated as follows:
TABLE IILubricating FluidComponentWeight %Polyol ester92.95Oligomeric amine antioxidant3.00Borate antiwear agent2.00Secondary antiwear agents2.00Corrosion inhibitor0.05Anti-foaming agent5 ppm
[0048] The resulting lubricant fluids had the following physical properties:
TABLE IIIRun 3Run 4Viscosity, cSt@ 100° C.:25.625.3@ 40° C.:386384Viscosity Index:8687Pour Point, ° C.:−20 (−5) −37 (−35)Flash Point, C.O.C., ° C.(° F.):310 (590)310 (590)Acid Valve, mgKOH / g:.36.38
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