Estolide compositions exhibiting high oxidative stability
A composition and compound technology, applied in lubricating composition, organic chemistry, fatty acid esterification, etc., can solve problems such as insufficient hydrolytic stability and oxidation stability
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Embodiment 1
[0236] The acid catalyst reaction was performed in a 50 gallon Pfaudler RT-Series glass lined reactor. Oleic acid (65Kg, OL700, Twin Rivers) was charged to the reactor along with 70% perchloric acid (992.3mL, Aldrich Cat#244252) and the reaction was carried out under vacuum (10 Torr absolute (Torr absolute; 1 Torr = ~1mmHg)). Heat to 60°C for 24 hours with continuous stirring. After 24 hours, the vacuum was released. 2-Ethylhexanol (29.97 Kg) was then added to the reactor and vacuum restored. The reaction was continued for another 4 hours under the same conditions (60 °C, 10 absolute Torr). At this point KOH (645.58 g) was dissolved in 90% ethanol / water (5000 mL, 90 vol% EtOH) and added to the reactor to quench the acid. The solution was then allowed to cool for about 30 minutes. The contents of the reactor were then pumped through a 1 μm (μ) filter into a collector to filter out the salts. Water is then added to the collector to wash the oil. The two liquid phases were ...
Embodiment 2
[0238] The acid catalyst reaction was performed in a 50 gallon Pfaudler RT-Series glass lined reactor. Oleic acid (50Kg, OL700, Twin Rivers) and full fraction coconut oil fatty acid (18.754Kg, TRC110, Twin Rivers) were added to the reactor with 70% perchloric acid (1145mL, Aldrich Cat#244252) and heated under vacuum (10 Absolute Torr) to 60° C. for 24 hours with continuous stirring. After 24 hours, the vacuum was released. 2-Ethylhexanol (34.58 Kg) was then added to the reactor and vacuum restored. The reaction was continued for another 4 hours under the same conditions (60 °C, 10 absolute Torr). At this point KOH (744.9 g) was dissolved in 90% ethanol / water (5000 mL, 90 vol% EtOH) and added to the reactor to quench the acid. The solution was then allowed to cool for about 30 minutes. The contents of the reactor were then pumped through a 1 μ filter into the collector to filter out the salts. Water is then added to the collector to wash the oil. The two liquid phases wer...
Embodiment 3
[0240] The estolide prepared in Example 1 (Example 1) was subjected to distillation conditions at 300° C. in a Myers 15 centrifugal still at an absolute pressure of about 12 μm (0.012 Torr). This produced a primary distillate with a lower EN average (Example 3A) and a distillation bottom with a higher EN average (Example 3B). Certain data are reported in Tables 1 and 8 below.
[0241] Table 1
[0242] estolide base stock
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