LUBE BASE OIL AND PROCESS FOR PREPARING THE SAME

Abstract: The present invention is a biodegradable lubricant base oil of good low-temperature fluidity and low cloud point, moreover good oxidative stability and lubricity, as well as its manufacturing process. The said lubricant base oil is manufactured by mixing and subjecting to an ester-exchange reaction 5 to 35% by weight of a fatty oil among constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid, 30 to 60% by weight of a fatty oil among constituent fatty acids of which there is 20% by weight or more of a trans-acid, and 15 to 45% by weight of either a fatty oil among constituent fatty acids of which there is 80% by weight or more of a medium-chain saturated fatty acid, or a medium-chain fatty acid or a lower alcohol ester thereof.

Description: Technical Field The present invention relates to lubricating oils suitable in rolling mill applications, in two- and four-cycle engine lubricating oil applications, and furthermore in cutting oil applications; in particular it relates to biodegradable lubricating oils having high oxidative stability, low-temperature fluidity and high lubricity. Background Art Among properties sought-after in a lubricating oil, the performance characteristics of (1) high oxidative stability, (2) satisfactory fluidity at low temperatures, (3) high viscosity index and (4) satisfactory lubricity in load-carrying capacity, anti-wear capacity, etc., can be given. Generally, mineral oils have been employed as oils in lubricants. In recent years, however, from an environmental preservation standpoint there have been calls centered in Europe for highly biodegradable oils, and the development of a base oil which replaces the poorly biodegradable mineral oils has been desired. As highly biodegradable base oils there are vegetable oils (the biodegradation rate according to the CEC-L33-A-93 method is 90-100%) and polyolesters (ditto, 55-100%). Vegetable fatty oils possess the drawback of inferior oxidative stability. Nevertheless, vegetable fatty oils have advantages such as high viscosity indices, excellent lubricity in extreme pressure, low volatility and good compatibility with additives. Accordingly, in recent years studies on improving the use of vegetable fatty oils in lubricant base oils have been made. For example, Pat. Laid-Open 209187, 1993 discloses a technology of improved cold resistance, i.e., low-temperature fluidity, by adding esters of polyglycerine fatty acid, esters of sucrose fatty acid, and lecithin to a liquid oil such as rapeseed oil. However, in the above-noted technology, because a liquid fat such as rapeseed oil is used, its oxidative stability is poor. Further, Laid-Open Pats. 14710, 1994 and 179882, 1995 disclose a technology of improved low-temperature fluidity that introduces a medium-chain saturated fatty acid into a liquid fat such as rapeseed oil by ester exchange. However, due to the use of a fatty oil such as rapeseed oil that contains a large quantity of unsaturated fatty acid, the oxidative stability is not good (e.g., in Laid-Open Pat. 179882, 1995, the Rancimatt stability is in the range of 4 to 5 hours). Meanwhile, there is also a technology that introduces a medium-chain saturated fatty acid into a hydrogenated coconut oil, palm kernel oil, etc. fatty oil whose unsaturated fatty acid content is scant (Laid-Open Pat. 314790, 1992). Nevertheless, although oxidative stability is improved with this technology, it turns out not to be satisfactory because solid fat is utilized and the cloud point is high (0 °C or more in the majority of instances). Therefore, in order to lower the cloud point, a large amount of expensive MCT becomes necessary. Fatty oils which become solid at ordinary temperatures, such as the foregoing palm oil, beef tallow and hardened oil, that are to be raw materials are of comparatively good oxidative stability, but since their melting points are high, their low-temperature fluidity is poor. Meanwhile, wherein a fatty oil such as linseed oil and fish oil which contains many highly unsaturated fatty aids, or a fatty oil such as rapeseed oil and soybean oil which contains much linolic acid, is utilized independently as a lubricating oil, it will be of comparatively good low-temperature fluidity, but the oxidative stability will be poor. As a fatty oil endowed concurrently with oxidative stability and low-temperature fluidity, medium-chain saturated fatty acid triglycerides (MCTs) can be given. However, wherein they are utilized independently, lubricity deteriorates, since compared with general vegetable oils (palm oil, rapeseed oil, etc.) the alkyl group is a short chain. In other words, a lubricating oil in which vegetable oil is made the base, and which is a base oil concurrently endowed with oxidative stability and low-temperature fluidity, at present has not yet been sufficiently developed. The object of the present invention is to develop a biodegradable lubricant base oil of good fluidity at low temperatures, of low cloud point, and furthermore of good oxidative stability and lubricity. Disclosure of the Invention As the result of zealous investigation in order to solve the above-noted problems, the present inventors, by discovering that among fatty oils of high oleic acid content, a fatty oil in which the trans-acid is made constant and in which medium-chain saturated fatty acids of 6 to 12 carbons are located into glyceride positions 1 and 3, is of good low-temperature fluidity, low cloud point, suitable lubricity and good oxidative stability, brought the present invention to completion. In other words, the present invention is a process for manufacturing a lubricant base oil, as well as a lubricant base oil obtained thereby, in which 5 to 35% by weight of a fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a diene fatty acid, 30 to 60% by weight of a fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid, and 15 to 45% by weight of either a fatty oil having constituent fatty acids of which there is 80% by weight or more of a medium-chain saturated fatty acid, or a medium-chain fatty acid or a lower alcohol ester thereof, are mixed and subjected to an ester-exchange reaction. The present invention further is a process for manufacturing a lubricant base oil, as well as a lubricant base oil obtained thereby, in which the above-noted fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid is a high-oleic sunflower oil. The present invention moreover is a process for manufacturing a lubricant base oil, as well as a lubricant base oil obtained thereby, in which the above-noted fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid is a hardened palm fractionated oil. The present invention is a process for manufacturing a lubricant base oil, as well as a lubricant base oil obtained thereby, in which the above-noted fatty oil having constituent fatty acids of which there is 80% by weight or more of a medium-chain saturated fatty acid is a MCT. The present invention is a process for manufacturing a lubricant base oil, as well as a lubricant base oil obtained thereby, in which the above-noted ester exchange reaction is carried out utilizing a lipase having specificity to glyceride positions 1 and 3. Most Preferable Form for Implementing the Present Invention As a fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid, high-oleic sunflower oil, hardened soybean fractionated oil and hardened rice bran oil can be given. Among these, high-oleic sunflower oil is especially preferable. If the said fatty oil is less than 5%, low-temperature fluidity worsens; if in excess of 35% by weight, oxidative stability worsens. Further, if the di-ene fatty acid surpasses 12% by weight, oxidative stability worsens. Accordingly, fatty oils in which the di-ene fatty acid content is large, such as rapeseed oil and sunflower oil, are excluded. As a fatty oil of 20% by weight or more trans-acid having its constituent fatty acids, hardened palm fractionated oil, hardened soybean fractionated oil and hardened fractionated rice bran oil can be given. If the fatty oil of 20% by weight or more trans-acid among its constituent fatty acids is less than 30% by weight oxidative stability worsens; if in excess of 60% by weight low-temperature fluidity worsens. A medium-chain saturated fatty acid in the present invention means a saturated fatty acid of 6 to 12 carbons. The number of carbons of the medium-chain fatty acid is preferably 8 to 10. A fatty oil which can be employed that contains 80% or more by weight medium-chain saturated fatty acid among its constituent fatty acids is the commercially available MCTs. If the fatty oil that contains 80% or more by weight medium-chain saturated fatty acid is less than 15% by weight, there will be problems with the low-temperature fluidity obtained; and if in excess of 45% by weight, the lubricity will be degraded. Mixing the foregoing fatty oils, an ester exchange reaction is carried out. The composition of the mixed oil is one which contains approximately 40-58% by weight mono-ene fatty acid, 10-20% by weight trans-acid and 20 to 40% by weight medium-chain saturated fatty acid. Due to the ester exchange reaction, the fatty oil submitted to the reaction has a low-temperature flow point and a low cloud point which could not be obtained only by simply mixing. This is because it is created from a mixed-acid group triglyceride into which medium-chain saturated fatty acids have been introduced. Accordingly, other than being introduced in the form of a triglyceride, the medium-chain saturated fatty acid can by introduced in the form of a lower alcohol ester of a medium-chain saturated fatty acid or a free medium-chain fatty acid. It is preferable to carry out the ester exchange with lipase having specificity to glyceride positions 1 and 3 as a catalyst. This is because random ester exchange easily invites elevation of cloud point, making necessary a post-reaction step in which the high melting-point component is removed fractionally. It is possible to utilize a publicly known lipase having specificity to glyceride positions 1 and 3. This may be exemplified, for example, by those that are microorganism derived, from Rhizopus delemar, Mucor miehei and Alcaligenes spp., etc.; and by those that are vegetable-oil derived, from soybean, rice bran and castor seed, etc. Other than such lipases as animal pancreatic lipase, it is also possible to utilize a fixed lipase obtained by ordinary adsorption, ionic or covalent bonding, or inclusion methods. Further, it is also suitable to utilize microorganisms such as fungi, yeasts and bacteria, that are capable of producing said lipase. The synthetic fatty oil can be used as is as a base oil in a lubricant. Depending on the stock oil, it may be suitable to carry out purifying treatments to remove acid, to decolor or to remove smell. Further, as needed, additives such as rust preventives, extreme-pressure agents, flow point lowering agents, oxidation preventives, defoaming agents, metal cleaners and anti-abrasion agents can be added; and it also can be used as a lubricant blended with ester series lubricating oils, mineral oils, or the like. Experiments (Embodiment 1) Hardened palm fractionated oil 54 % by weight High-oleic sunflower oil 6 % by weight MCT 40 % by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. As to the hardened palm fractionated oil, the low-melting point part of an oil in which the palm olein was hardened and fractionated was utilized (33% by weight trans-acid, 64% by weight mono-ene fatty acid of 16 or more carbons, 4.3% di-ene fatty acid of 16 or more carbons). The mono-ene fatty acid content in the high-oleic sunflower oil was 81% by weight, and the di-ene fatty acid of 16 or more carbons was 8.8% by weight. The MCT utilized was one having a C8=65% and C10=35% composition. Embodiment 2 Hardened palm fractionated oil 50% by weight High-oleic sunflower oil 30% by weight MCT 20% by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. Embodiment 3 Hardened palm fractionated oil 40% by weight High-oleic sunflower oil 20% by weight MCT 40% by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. The hardened soybean fractionated oil utilized was one having a 35% by weight trans-acid, 77% by weight mono-ene fatty acid of 16 or more carbons, and 7.5% by weight di-ene fatty acid of 16 or more carbons composition. Comparative Example 1 Oil blend of Example 1 (ester exchange not carried out). Comparative Example 2 Oil blend of Example 2 (ester exchange not carried out). Comparative Example 3 Oil blend of Example 3 (ester exchange not carried out). Comparative Example 4 Hardened palm fractionated oil 67.5% by weight High-oleic sunflower oil 7.5% by weight MCT 25% by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. Comparative Example 5 Hardened palm fractionated oil 20.0% by weight High-oleic sunflower oil 60.0% by weight MCT 20.0% by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. Comparative Example 6 Hardened palm fractionated oil 40.0% by weight High-oleic sunflower oil 30.0% by weight MCT 30.0% by weight Utilizing 1, 3 specific lipase (derived from Rhizopus niveus) an ester exchange reaction was carried out on the above-noted blended oil. (Experimental Results) The fatty oil compositions obtained in the embodiments and comparative examples are shown in Table 1. % Mono-ene Patty Acid Among Fatty Acid Constituents % Trans-Acid Among Fatty Acid Constituents Embodiment 1 43.8 18.0 Embodiment 2 56.1 16.7 Embodiment 3 45.2 14.1 Compar. Ex. 1 43.8 18.0 Compar. Ex. 2 56.1 16.7 Compar. Ex. 3 45.2 14.1 Compar. Ex. 4 49.2 22.5 Compar. Ex. 5 60.8 6.7 Compar. Ex. 6 36.7 13.3 In order to conduct an evaluation of the fatty oils of the present invention, the measurements below were carried out. The results are shown in Table 2. (1) Pour point and cloud point: carried out by an automatic pour point/cloud point measuring apparatus (Tanaka Scientific Instruments mfr.) on the basis of JIS K2269. (2) Oxidative stability (RBOT oxidative stability): carried out by a rotary-bomb type oxidative stability testing appliance (Rigou Co. Mfr.) on the basis of JIS K2514. Rancimat stability: measured by a measuring device of Switzerland Metrohm Co. mfr. (3) Viscosity index: carried out on the basis of ASTM D2270-64. Pour Point Cloud Point Rancimat Stability (hr) RBOT Oxidative Stability (min) viscosity Index Embodiment 1 -5.0 -3.1 45.3 63 148 Embodiment 2 -6.0 -3.2 31.4 34 150 Embodiment 3 -2.0 -4.0 37.0 57 155 Compar. Ex. 1 -1.0 22.9 49.6 85 154 Compar. Ex. 2 -1.0 15.7 35.3 60 152 Compar. Ex. 3 2.0 12.1 40.3 71 156 Compar. Ex. 4 -1.0 10.5 36.2 38 148 Compar. Ex. 5 -14.0 -4.0 10.3 16 152 Compar. Ex. 6 5.07 15.1 22.5 21 152 Rapeseed Oil -18.0 -12.3 3.2 11 148 High-Oleic Sunflower oil -9.0 40.0 9.0 15 152 The embodiments, being of low pour points and cloud points, moreover of high oxidative stability, proved to be satisfactory. The oxidative stability is extremely high compared with rapeseed oil and high-oleic sunflower oil. Comparative examples 1 to 3 turned out to have high flow points and cloud points because ester exchange was not carried out. Further, comparative example 4 is of good stability since the trans-acid is plentiful, but the pour point and cloud point turned out to be high. Comparative example 5 is of poor stability since the trans-acid is scant and the mono-ene fatty acid is plentiful. Comparative example 6 turned out to be of high flow point and cloud point since the mono-ene fatty acid was scarce. Industrial Applicability According to the foregoing, a lubricant base oil manufacturing process in connection with the present invention, as well as a lubricant base oil obtained thereby, are a method of introducing medium-chain saturated fatty acids of 6 to 12 carbons into the 1, 3 positions of glyceride in vegetable fatty oils containing many mono-ene fatty acids as well as vegetable oils of 20% or more trans-acid content among the constituent fatty acids, and a lubricant base oil obtained thereby, which can provide good oxidative stability, good low-temperature fluidity and a low cloud point.

Claims: A process for manufacturing a lubricant base oil, characterized in that : 5 to 35% by weight of a fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid, 30 to 60% by weight of a fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid, and 15 to 45% by weight of either a fatty oil having constituent fatty acids of which there is 80% by weight or more of a saturated fatty acid of 6 to 12 carbons, or a fatty acid of 6 to 12 carbons or a lower alcohol ester thereof, are mixed; and subjected to an ester-exchange reaction. A process for manufacturing a lubricant base oil as set forth in claim 1, wherein said fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid is a high-oleic sunflower oil. A process for manufacturing a lubricant base oil as set forth in claim 1, wherein said fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid is a hardened palm fractionated oil. A process for manufacturing a lubricant base oil as set forth in claim 1, wherein said fatty oil having constituent fatty acids of which there is 80% by weight or more of a saturated fatty acid of 6 to 12 carbons is a MCT. A process for manufacturing a lubricant base oil as set forth in claim 1, wherein said ester exchange reaction is carried out utilizing a lipase having specificity to glyceride positions 1 and 3. A lubricant base oil obtained by means of an ester exchange reaction done mixing 5 to 35% by weight of a fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid; 30 to 60% by weight of a fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid; and 15 to 45% by weight of either a fatty oil having constituent fatty acids of which there is 80% by weight or more of a saturated fatty acid of 6 to 12 carbons, or a fatty acid of 6 to 12 carbons or a lower alcohol ester thereof. A lubricant base oil as set forth in claim 6, wherein said fatty oil having constituent fatty acids of which there is 60% or more by weight of a mono-ene fatty acid having 16 or more carbons and 12% or less by weight of a di-ene fatty acid is a high-oleic sunflower oil. A lubricant base oil as set forth in claim 6, wherein said fatty oil having constituent fatty acids of which there is 20% by weight or more of a trans-acid is a hardened palm fractionated oil. A lubricant base oil as set forth in claim 1, wherein said fatty oil having constituent fatty acids of which there is 80% by weight or more of a saturated fatty acid of 6 to 12 carbons is a MCT. A lubricant base oil as set forth in claim 6, wherein said ester exchange reaction is carried out utilizing a lipase having specificity to glyceride positions 1 and 3.

Inventors: IBUKI MASAHISA, NAGAOKA SHUSHI, IBUKI, MASAHISA, NAGAOKA, SHUSHI, IBUKI, Masahisa, Fuji Oil Co., Ltd., NAGAOKA, Shushi, Fuji Oil Co., Ltd.
Applicants: FUJI OIL CO LTD, FUJI OIL COMPANY, LIMITED
Application year: 1997
Main classification: C10M105
IPC codes: C10M105, C10M109