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Estolide derivatives useful as biolubricants

An acid anhydride and product technology, applied in the field of biological lubricant compositions, can solve problems such as not showing thermal oxidation stability

Inactive Publication Date: 2014-03-19
DOW GLOBAL TECH LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0010] However, none of the above methods have been shown to produce a fully saturated material with the ideal combination of low pour point (at or below -10°C), thermo-oxidative stability and renewable carbon (at least 50% by weight)

Method used

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  • Estolide derivatives useful as biolubricants
  • Estolide derivatives useful as biolubricants
  • Estolide derivatives useful as biolubricants

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preparation example Construction

[0030] The preparation of anhydride derivatives can be carried out starting from mixtures of hydroxylated fatty acids or fatty acid esters. It has surprisingly been found that, starting from such mixtures, anhydride derivatives can be prepared which exhibit advantageous properties, including a very low pour point, according to the process of the invention. Accordingly, the anhydride derivatives may be suitable for a wide range of applications, including those requiring properties at very low temperatures.

[0031] In some embodiments, the mixture of starting hydroxylated fatty acids or fatty acid esters comprises two or more hydroxylated C 1 -C 24 Fatty acids, or two or more hydroxylated C 1 -C 20 Fatty acids (or their esters). In some embodiments, the mixture comprises short chain hydroxylated fatty acids, such as hydroxylated C 1 -C 4 -COOH (or its esters) and long-chain hydroxylated fatty acids such as hydroxylated C 12 -C 20 -COOH (or its esters). In a preferred e...

Embodiment 1

[0060] Step 1: A glass reactor equipped with a temperature controller, overhead stirrer, and Dean-Stark apparatus was loaded with 12-hydroxy-stearic acid (450.4 grams (g)), lactic acid (37.1 g), 2-ethylhexanol ( 487.8g) and tin(II) 2-ethylhexanoate (1.9g). The mixture was then heated to 190°C for a period of 6 hours while removing water by fractional distillation. Excess 2-ethylhexanol was removed by distillation under reduced pressure at 160°C, and then the reactor was cooled to 120°C.

[0061] Step 2: To the product of Step 1 (584.7 g) was added tin(II) 2-ethylhexanoate (1.2 g). The mixture was heated to the set point temperature of 200° C. for a period of three hours with stirring. Excess 2-ethylhexanol was removed from the reactor contents by distillation under reduced pressure (20 mbar), and the reactor was then cooled to 120°C.

[0062]Step 3: To the product of Step 2 (466.2 g) was added isobutyric anhydride (120.4 g). The reactor was stirred at this temperature for ...

Embodiment 2

[0064] Step 1: A glass reactor equipped with a temperature controller, overhead stirrer and Dean-Stark apparatus was loaded with 12-hydroxy-stearic acid (407.0 g), lactic acid (67.6 g), 2-ethylhexanol (520.2 g) and tin(II) 2-ethylhexanoate (2.0 g). The mixture was heated to a set point temperature of 190°C and kept stirring for a period of 6 hours, water was removed by fractional distillation. Excess 2-ethylhexanol was removed by distillation under reduced pressure at 160°C, and then the reactor was cooled to 120°C.

[0065] Step 2: To the Step 1 product (565.8 g) was added tin(II) 2-ethylhexanoate (1.3 g) and the mixture was heated to a set point temperature of 200° C. for a period of three hours with stirring. 2-Ethylhexanol formed during the reaction was removed from the reactor contents by distillation under reduced pressure (20 mbar), and the reactor was then cooled to 120°C.

[0066] Step 3: To the product of Step 2 (445.0 g) was added isobutyric anhydride (144.3 g). ...

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Abstract

A composition comprising a mixture of esters prepared by a three-step process comprising the steps of a oligomerization, a transesterification, and a capping, The composition is useful in a variety of applications, including as a biolubricant having a high level of renewable carbons, and may exhibit particularly desirable properties relating to pour point, thermo-oxidative stability, and viscometric behavior due to reduced or eliminated levels of unsaturation in the final double esters.

Description

[0001] Cross References to Related Applications [0002] This application claims priority to Provisional Application Serial No. 61 / 501,802, filed June 28, 2011, which is hereby incorporated by reference in its entirety. field of invention [0003] The present invention relates to biolubricant compositions. More specifically, the present invention relates to estolide derivatives of fatty acids, which have high levels of renewable raw materials and are useful as lubricants. Background technique [0004] Currently, the lubricant (engine and non-engine) and process fluid industries are searching for biodegradable materials. Biodegradability refers to the degradation of lubricants and process fluids (hereafter referred to as "fluids") over a period of time, which can be measured by tests, for example, by the Organization of Economic Co-Operation and Development (Organization of Economic Co-Operation and Development) (OECD) promulgated tests, including OECD301B and OECD301F. R...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10M105/42C07C69/675C11C3/00
CPCC11C3/08C10M2207/301C10M105/42C11C3/14C10N2230/02C11C3/003C10N2230/10C10N2220/025C10M105/36C10N2220/022C10N2270/00C10N2220/024C10N2230/64C10N2220/10C10N2020/013C10N2020/065C10N2020/081C10N2020/02C10N2030/02C10N2030/10C10N2030/64C10N2070/00
Inventor D·芬奇J·科尔斯布尔克M·R·格瑞维斯
Owner DOW GLOBAL TECH LLC