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Methods for concentration and extraction of lubricity compounds and biologically active fractions from naturally derived fats, oils and greases

a technology of biologically active fractions and lubricity compounds, which is applied in the production of fatty-oils/fats, fuel additives, liquid carbonaceous fuels, etc., can solve the problems of lubricity problems, increase the wear and fretting wear of sliding adhesives of pump components, and low sulfur diesel fuels. achieve the effect of reducing the level of biologically active components

Inactive Publication Date: 2007-06-07
AGRI & AGRI FOOD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The present invention relates to a method for producing a concentrate of lubricity additives from triglyceride-containing materials, such as fats, oils, and greases. The method involves converting the triglyceride components of the material to lower molecular weight compounds, such as fatty acids, fatty amides, or fatty alcohols, through a process of distillation. The resulting mixture contains ingredients with higher lubricity than the original material. The invention also includes methods for pre-extracting the oil to concentrate specific components with biological activity, such as phytosterol, tocopherols, and carotenoids. The concentrate can be used as a lubricity additive in various applications."

Problems solved by technology

The reduction in the sulfur content of diesel fuel has resulted in lubricity problems.
Low sulfur diesel fuels have been found to increase the sliding adhesive wear and fretting wear of pump components such as rollers, cam plate, coupling, lever joints and shaft drive journal bearings.
Reducing the level of one or more of the sulfur, polynuclear aromatic or polar components of diesel fuel oil can reduce the ability of the oil to lubricate the injection system of the engine.
As a result of poor fuel lubrication properties the fuel injection pump of the engine may fail relatively early in the life of an engine.
Failure may occur in fuel injection systems such as high-pressure rotary distributors, in-line pumps and injectors.
The problem of poor lubricity in diesel fuel oils is likely to be exacerbated by future engine developments, aimed at further reducing emissions, which will result in engines having more exacting lubricity requirements than present engines.
Similarly, poor lubricity can lead to wear problems in other mechanical devices dependent for lubrication on the natural lubricity of fuel oil.
While the biologically active components may occur at concentrations sufficient to impart useful biological responses their concentrations are often insufficient for many applications.
Nevertheless, the concentrations found in most sources are less than sufficient to produce a therapeutic effect.
While vegetable oils are significant sources of vitamin E in the diet levels may be inadequate to meet recommended daily allowances and recommended levels for therapeutic effects.
While vegetable oils may be rich sources of sterol esters, tocols, and carotenoids methods of recovery of these components are inefficient and products must be fractionated and reformulated for use.

Method used

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  • Methods for concentration and extraction of lubricity compounds and biologically active fractions from naturally derived fats, oils and greases
  • Methods for concentration and extraction of lubricity compounds and biologically active fractions from naturally derived fats, oils and greases
  • Methods for concentration and extraction of lubricity compounds and biologically active fractions from naturally derived fats, oils and greases

Examples

Experimental program
Comparison scheme
Effect test

example 1

Two Stage Transesterification of Canola Oil with Methanol and Potassium Hydroxide

[0077] Methyl esters of canola oil, also known to those skilled in the art as low erucic acid rapeseed oil, were prepared using a two-stage base catalysed transesterification. The two-stage reaction was required to remove glyceride from the final product. Prior to the reaction the catalyst was prepared by dissolving potassium hydroxide (10 g) in methanol (100 g). The catalyst solution was divided into two 55 g fractions and one fraction was added to 500 g of canola oil (purchased from a local grocery store) in a 1 L beaker. The oil, catalyst and methanol were covered and stirred vigorously for 1 hour on a stirring hot plate by the addition of a teflon stirring bar. After stirring, the contents of the beaker were allowed to settle for 2 hours. At this time a cloudy upper layer and a viscous lower layer had separated. The layers were separated using a seperatory funnel and the upper layer was mixed with ...

example 2

Two Stage Transesterification of Tallow with Methanol and Potassium Hydroxide

[0078] Tallow was collected from a renderer. Five hundred grams of tallow were heated to 40° C. prior to esterification to liquify the solid mass. Thereafter, all processes and conditions were identical to those described in example 1.

example 3

Refining and Distillation of Canola Oil Methyl Ester

[0079] Canola methyl ester prepared in example 1 was refined to remove methanol, glycerol, soaps and other compounds that might interfere with distillation. Methanol was removed under vacuum (28.5″) by a rotary vacuum evaporator equipped with a condenser. The methyl esters were maintained at 50° C. for 30 minutes to thoroughly remove alcohol. After evaporation the esters were treated with silica (0.25% w / w Trisyl 600; W. R. Grace Co.) and stirred at room temperature for 1 hour. After silica treatment methyl esters were filtered over a bed of Celite to remove both silica and other materials.

[0080] After refining the methyl esters, fractional high vacuum distillation was performed using a simple distillation apparatus. A vacuum of less than 1 mm was maintained throughout the procedure. During fractionation temperatures at the top of the column, before the condenser, were between 120° C. and 140° C. The distillation apparatus includ...

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Abstract

Methods for recovery of concentrates of lubricating compounds and biologically active compounds from vegetable and animal oils, fats and greases that allow separation of triglycerides, from components with higher lubricity or biological activity or enrichment protocols that increase the concentration of high lubricity or biologically active compounds in the triglyceride. The triglycerides are transesterified with a lower alcohol to produce alkyl esters. Following the conversion process the esters are separated from high molecular weight high lubricity compounds and biologically active compounds by distillation. The esters have some lubricity and may be sold as pollution reducing fuel components. The high boiling point compounds that are the residues of distillation, however, can either contribute significant lubricity and may be used widely in lubricant applications or added to petroleum fuels to decrease friction or the biologically active components may be used in nutritional, cosmetic and therapeutic applications. Therapeutic applications include use in human diets to lower cholesterol.

Description

CROSS REFERENCE TO RELATED APPLICATION [0001] This application is a Continuation-in-part of previously filed U.S. patent application Ser. No. 11 / 290,781 filed 1 Dec. 2005FIELD OF INVENTION [0002] The present invention relates to methods for producing a high lubricity fraction and for producing bioactive fractions from fats, oils and greases derived from a wide variety of animal and vegetable sources. In this specification, the terms “oils, fats and greases” are used synonymously to describe starting materials derived from vegetable and animal sources. Oils tend to be liquid at room temperature and are derived from many biological sources such as whales, fish and oil seed. Fats are generally solid at room temperature and are derived from the same sources as oils. Greases usually have high melting points and they may be synthetic products. Some synthetic greases are plant derived, others are from animals. The novel methods either separate lower lubricity components of the fat, oil, or...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C10L1/18
CPCC10L1/1802C10L1/1817C10L1/19C10L10/08C10M105/34C10M159/02C10M159/08C10M177/00C10M2207/2815C10M2207/40C10N2270/00C11B1/06C11B1/10C11B3/001C11C3/003C10N2070/00
Inventor REANEY, MARTIN J.PIETTE, GABRIELLEHERTZ, PHILIP BARRYWESTCOTT, NEIL D.
Owner AGRI & AGRI FOOD