CN114507138A - Ester compound and preparation method and application thereof - Google Patents

Ester compound and preparation method and application thereof Download PDF

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CN114507138A
CN114507138A CN202011167141.4A CN202011167141A CN114507138A CN 114507138 A CN114507138 A CN 114507138A CN 202011167141 A CN202011167141 A CN 202011167141A CN 114507138 A CN114507138 A CN 114507138A
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group
acid
integer
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韩天昊
梁宇翔
刘辉
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Sinopec Research Institute of Petroleum Processing
China Petroleum and Chemical Corp
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Sinopec Research Institute of Petroleum Processing
China Petroleum and Chemical Corp
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/612Esters of carboxylic acids having a carboxyl group bound to an acyclic carbon atom and having a six-membered aromatic ring in the acid moiety
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/08Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing oxygen
    • C10M105/32Esters
    • C10M105/34Esters of monocarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/284Esters of aromatic monocarboxylic acids

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Abstract

The invention provides an ester compound and a preparation method and application thereof. The structure of the ester compound is shown as the formula (I):

Description

Ester compound and preparation method and application thereof
Technical Field
The present invention relates to the field of lubricant products, and in particular to ester compounds suitable for use as lubricating base oils.
Background
With the development of engine and other mechanical equipment technologies, the use conditions of lubricating oil are increasingly harsh, the lubricating oil industry faces serious challenges of quality upgrading, economic benefits and environmental regulations, and high-quality lubricating oil base oil with excellent thermal oxidation stability, hydrolytic stability, high viscosity index and low volatility is urgently required to be produced. The market demand has driven the research on high quality base oils, wherein synthetic or semi-synthetic oils, with their excellent and unique properties, have made up for the deficiencies in mineral oil properties in many fields and are increasingly used more widely.
The oxidation stability refers to the high-temperature oxidation resistance and high-temperature deposition alleviation capability of the lubricating oil in the using process, and is an important embodiment of the high-temperature oxidation resistance of the lubricating oil. The lubricating oil has harsh working conditions and complex oxidation process. The oxidation reaction is closely related to the chemical composition of the lubricant base oil, the working environment, and the internal architecture of the engine. The oxidation stability of the base oil of the lubricating oil is poor, a series of chemical changes such as oxidation, polymerization, alkylation, decomposition and the like occur in a short period under the induction of high-temperature oxygen and the catalytic action of metals, so that the physicochemical properties and the color appearance of the engine oil are changed, such as increase of total acid value, increase of viscosity, deepening of color, low heat transfer efficiency, emulsification and foam generation, so that the service performance of the oil product is greatly reduced, and a large amount of generated oil sludge and other sediments are attached to metal accessories, so that piston ring sticking and equipment severe corrosion are caused, the abrasion of parts is increased, the working efficiency of mechanical equipment is reduced, the service life of the equipment is shortened, and even the normal working operation of the engine is seriously influenced. Improving the oxidation stability of the base oil of the lubricating oil has important significance for improving the working efficiency and the service life of lubricating system equipment.
The alkyl aromatic base oil is a high-performance base oil or a base oil blending component, has more excellent thermal oxidation stability and good additive solubility compared with mineral oil, PAO oil and ester oil, can be compatible with various sealing materials, and effectively provides a technical means for blending high-performance lubricating oil. The use of alkyl aromatic base oils as blendstocks can exhibit better performance properties than ester oil/PAO oil blended lubricants. Moreover, the blending of alkyl aromatic base oil into mineral oil can significantly increase the service temperature of mineral oil, and the use of alkyl aromatic base oil components in some foreign high-grade lubricating oils has been reported. Therefore, the alkyl aromatic base oil is valued by a plurality of big foreign companies, and the product production technology has high requirements and few published documents, so that the alkyl aromatic base oil becomes a high-added-value product monopolized by the big foreign companies, and the domestic blank is still a blank in this respect at present. Therefore, the alkyl aromatic base oil has very good development and application prospects, particularly has the characteristic of excellent thermo-oxidative stability of the alkyl aromatic base oil in some high-temperature aerobic working environments, and can also be used for producing special industrial oil, such as carbon dioxide refrigerator oil and the like.
The excellent oxidation stability of alkyl aromatic base oils depends mainly on the aromatic rings in the molecular structure. Therefore, the oxidation stability of the lubricating oil is effectively improved, the aryl base oil component with good oxidation stability and excellent other physical and chemical properties can be adopted, the generation of oxidation products can be effectively reduced, and the oxidation stability is improved.
US 4035308 discloses the use of AlCl subjected to anhydrous treatment3The monosubstituted alkyl aromatic hydrocarbon is synthesized and used as a blending component of the lubricating oil.
US 4148834 discloses a lubricant base oil component having as a major component a disubstituted long chain alkyl aromatic hydrocarbon. The component is prepared by a two-step alkylation method, wherein in the first step of alkylation, HF is used as a catalyst to catalyze the alkylation reaction of aromatic hydrocarbon and long-chain alpha-olefin, and in the second step, AlCl is used3Or AlBr3Instead of HF as catalyst.
US 5254766 discloses the synthesis of long chain alkyl naphthalenes and their derivatives using heteropolyacids (phosphotungstic or silicotungstic acids) as catalysts.
US 6596662 discloses the preparation of hexadecyl naphthalene (olefin conversion: 92.4%, wherein monoalkyl naphthalene accounts for 85.8%, dialkyl naphthalene accounts for 6.6%), hexadecyl diphenyl sulfide (olefin conversion 84.8%, wherein monoalkyl substituent accounts for 79.7%, dialkyl substituent accounts for 5.1%), hexadecyl diphenyl ether (olefin conversion 91.5%, wherein monoalkyl diphenyl ether accounts for 88.8%, dialkyl diphenyl ether accounts for 2.7%) using a dealuminated USY molecular sieve (silicon-aluminum atomic ratio 6.5-10, aluminum content outside the framework < 25%).
CN 1225617a discloses that an amine ionic liquid is used to catalyze the alkylation reaction of benzene and dodecene at room temperature, the selectivity of the reaction is 87%, the conversion rate of dodecene is more than 98%, and compared with the product obtained by the commonly used HF method, the product obtained by using the ionic liquid has better distribution of isomers and more 2-position substitution products.
WO99/03163 discloses the passing of ionic liquids through impregnationMethod for immobilizing on porous polymer and SiO2The novel alkylation catalyst is prepared from materials such as powder, porous alumina, molecular sieve, clay and the like, and has the advantages of high catalytic activity, high reaction speed and high 2-alkylbenzene content. Compared with the single use of the ionic liquid catalyst, the catalyst has improved stability, and the recycling frequency is greatly higher than that of the ionic liquid catalyst.
Despite the better oxidation stability of the existing alkyl aromatic base oils, there is still much room for improvement. There remains a need in the art for alkyl aromatic base oils that have superior properties.
Disclosure of Invention
The invention provides an ester compound and a preparation method and application thereof.
The structure of the ester compound is shown as the formula (I):
Figure BDA0002746174020000031
in the formula (I), Ar ring group is C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthracenyl);
n is an integer of 1 to 20 (preferably an integer of 1 to 15, more preferably an integer of 1 to 10, and further preferably an integer of 1 to 6);
n R groups are bonded to the Ar ring group;
n R groups are each independently selected from the group of formula (II), C1~30Is preferably independently selected from the group represented by the formula (II), C1~20More preferably, each of the straight-chain or branched alkyl groups and H is independently selected from the group represented by the formula (II), C1~10H) and at least one R group is selected from the group represented by formula (II);
Figure BDA0002746174020000032
in the formula (II), m is an integer of 1 to 10 (preferably an integer of 1 to 5, more preferably 1, 2 or 3); r1The radicals being selected from C1~30Is preferably selected from C1~20More preferably selected from C1~10Straight or branched alkyl groups of (ii); m R2Each independently selected from C1~30Alkylene group of (2), a single bond (preferably selected from C)1~20Is more preferably selected from C1~10Linear or branched alkylene, single bond, with
Figure BDA0002746174020000033
Bonded R2The radicals are preferably selected from C1~10Linear or branched alkylene groups of (a); r3The radicals being selected from C1~30Is preferably selected from C, H1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H);
m a 'groups are each independently selected from-CH ═ CH-, ethylene-, a group represented by formula (III), a group represented by formula (IV), a group represented by formula (V) and a group represented by formula (VI), and at least one a' group present in formula (II) is selected from a group represented by formula (III) or a group represented by formula (IV), the group represented by formula (III) or formula (IV) is bonded to the Ar ring group in formula (I), and represents a bonding end at which the group represented by formula (III) or formula (IV) is bonded to the Ar ring group in formula (I);
Figure BDA0002746174020000041
in the group represented by the formula (III), the group represented by the formula (IV), the group represented by the formula (V) and the group represented by the formula (VI), each R4Each independently selected from C1~30Is preferably selected from C, H1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H); ar ring radical being C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthryl)。
The ester compound of the invention comprises one compound or a plurality of compounds mixed in any proportion as follows:
Figure BDA0002746174020000042
the invention also provides a preparation method of the ester compound, which comprises the step of reacting the compound shown in the formula (alpha) with the compound shown in the formula (beta),
Figure BDA0002746174020000051
in the formula (. alpha.), m is an integer of 1 to 10 (preferably an integer of 1 to 5, more preferably 1, 2 or 3); r is1The radicals being selected from C1~30Is preferably selected from C1~20More preferably selected from C1~10Straight or branched alkyl groups of (ii); m R2Each independently selected from C1~30Alkylene group of (2), a single bond (preferably selected from C)1~20Is more preferably selected from C1~10A straight or branched alkylene group of (A), a single bond, and
Figure BDA0002746174020000052
bonded R2The radicals are preferably selected from C1~10Linear or branched alkylene groups of (a); r3The radicals being selected from C1~30A hydrocarbon group of (C), H (preferably selected from C)1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H);
in the formula (. beta.), Ar ring group is C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthracenyl); n' is an integer of 1 to 19 (preferably an integer of 1 to 14, more preferably an integer of 1 to 9, and further preferably an integer of 1 to 5);
n 'R' groups are bonded to the Ar ring group;
n 'R' groups are each independently selected from C1~30Is preferably independently selected from C1~20More preferably each is independently selected from C1~10Straight or branched alkyl, H).
According to the preparation method of the present invention, the compound represented by the formula (α) may be one or more selected from the following compounds: octenoic acid, decenoic acid, undecenoic acid, dodecenoic acid, decatetraenoic acid, hexadecenoic acid, oleic acid, linoleic acid, linolenic acid, and eicosenoic acid.
According to the preparation method of the present invention, the compound represented by the formula (β) may be one or more selected from the following compounds: benzene, naphthalene, anthracene, methylnaphthalene, ethylnaphthalene, n-propylnaphthalene, 2-isopropylnaphthalene.
According to the production method of the present invention, the mass ratio between the compound represented by the formula (α) and the compound represented by the formula (β) is preferably 1: 0.1 to 1; more preferably 1: 0.2 to 1.
According to the preparation method of the present invention, the temperature for reacting the compound represented by the formula (α) with the compound represented by the formula (β) is preferably 60 to 200 ℃, more preferably 90 to 180 ℃.
According to the preparation method of the present invention, the reaction time of the compound represented by the formula (α) and the compound represented by the formula (β) is generally as long as possible, and is preferably 1 to 8 hours, and more preferably 3 to 6 hours.
According to the production method of the present invention, preferably, the compound represented by the formula (α) is reacted with the compound represented by the formula (β) in the presence of an inert gas, preferably nitrogen.
According to the preparation method of the present invention, a catalyst may be added or not added, preferably a catalyst is added in the reaction of the compound represented by the formula (α) and the compound represented by the formula (β). The catalyst is preferably an acidic catalyst, and for example, a Lewis acid, a transition metal salt, a metal oxide,
Figure BDA0002746174020000061
One or more of acid, solid acid, acidic ionic liquid and supported catalyst thereof, wherein the supported catalyst can be a carrierAs molecular sieve, alumina, zeolite, graphite, carbon black, resin. The acid catalyst can be one or more of aluminum trichloride, stannic chloride, boron trifluoride, sulfuric acid, hydrofluoric acid, phosphoric acid, Y-type molecular sieve, M-type molecular sieve, beta zeolite, mordenite, phosphotungstic acid, silicon aluminum fluoride and perfluoroalkanesulfonic acid and a supported catalyst thereof. The amount of the catalyst is preferably 1% to 10% of the amount of the compound represented by the formula (α).
According to the preparation method of the present invention, a solvent may be added or may not be added, preferably a solvent is added in the reaction of the compound represented by the formula (α) and the compound represented by the formula (β). The solvent is preferably a hydrocarbon solvent, preferably one or more of alkane, aromatic hydrocarbon and ether, more preferably an alkane solvent, and for example, one or more of hexane, heptane, octane, nonane, decane, cyclohexane, cycloheptane, cyclooctane, cyclononane, cyclodecane, benzene, toluene, xylene, ethylbenzene, propylbenzene, diethyl ether, propyl ether, isopropyl ether and dibutyl ether may be used. The amount of the solvent to be added is not particularly limited, as long as the reaction is promoted to proceed smoothly. The solvent may be removed by a known method, for example, distillation, rectification, or the like, and is not particularly limited.
According to the preparation method of the invention, the reaction product is optionally washed and purified by using a solvent, and the solvent which can be washed is preferably a hydrocarbon solvent. The solvent may be removed by a conventional technique such as drying, evaporation, distillation, etc., and is not particularly limited.
The ester compound prepared by the preparation method can be a compound with a single structure or a mixture containing compounds with different structures. For a mixture of compounds of different structures, it is sometimes possible to separate it into compounds of a single structure, and it is sometimes also possible to use the mixture of compounds of different structures as it is without separating it into compounds of a single structure.
The product obtained by the production method of the present invention may contain, in addition to the ester compound, an unreacted compound represented by the formula (α) and/or a compound represented by the formula (β), and sometimes, for economic reasons, the unreacted compound represented by the formula (α) and/or the compound represented by the formula (β) are not separated from the product, but a mixture thereof is directly used as a product.
The ester compound can obviously improve the oxidation stability of lubricating oil (especially synthetic lubricating oil), and is suitable for being used as lubricating base oil.
The invention also provides a lubricating oil composition which comprises the ester compound or the ester compound prepared by the method and a lubricating oil additive. Wherein the ester compound accounts for 10-99%, preferably 30-95%, more preferably 50-90% of the total mass of the lubricating oil composition. Examples of the lubricating oil additive include various additives that are allowed to be added to a lubricating oil composition in the art, and specific examples thereof include an antioxidant, a detergent, a dispersant, a pour point depressant, a viscosity index improver, a friction modifier, an extreme pressure agent, an antiwear agent, and an antifoaming agent. The kind and amount of these additives are well known to those skilled in the art and will not be described herein. These additives may be used singly or in combination in any ratio.
The lubricating oil composition of the present invention has excellent oxidation stability.
Detailed Description
In the context of the present specification, the term "single bond" is sometimes used in the definition of a group. By "single bond", it is meant that the group is absent. For example, assume the formula-CH2-A-CH3Wherein the group a is defined as being selected from the group consisting of a single bond and a methyl group. In this respect, if A is a single bond, this means that the group A is absent, in which case the formula is correspondingly simplified to-CH2-CH3
The present invention will be further illustrated in detail by the following examples and comparative examples, but the present invention is not limited thereto.
The main raw materials used are from the following sources:
10-undecylenic acid methyl ester, Iknoka science and technology Co., Ltd, Beijing, analytical purity
Refined naphthalene, national chemical group chemical reagent Limited, analytical pure
Aluminum trichloride, national pharmaceutical group chemical reagent Co., Ltd, analytical purity
N-heptane, national chemical group chemical reagent Limited, analytical pure
Sodium hydroxide, national pharmaceutical group chemical reagents, Inc., analytical purity
1-methylnaphthalene, national pharmaceutical group chemical reagents, Ltd, analytical purity
Y-type molecular sieve, catalyst factory of southern Kai university, industrial products
Boron trifluoride etherate, analytical purity, Ikay technologies, Beijing
Trifluoromethanesulfonic acid, Beijing YinoKay science and technology Co., Ltd, analytically pure
Alkylnaphthalenes, Shanghai Nake science and technology Co., Ltd, Industrial products
T501, department of petrochemical industry, institute of research, Xinpu corporation, Industrial products
T511, department of petrochemical industry, institute of research, Xinpu corporation, Industrial products
Mineral oil S6, China petrochemical lubricating oil Co., Ltd., Industrial products
Example 1
A1L round-bottom flask was charged with 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane, and the mixture was heated to 70 ℃ with stirring. After naphthalene was completely dissolved, 3.46g of aluminum trichloride was added to the mixture, and stirring and heating were continued to 90 ℃ while introducing nitrogen gas, and reaction was carried out at 130 ℃ for 3 hours while maintaining good reflux of n-heptane. And when the reaction liquid is cooled to about 50 ℃, closing the nitrogen protection, and removing the solid catalyst by vacuum filtration to obtain dark brown oily liquid. Respectively carrying out alkali washing and water washing 3 times by using 0.1mol/L sodium hydroxide solution and deionized water, separating a water phase and an oil phase by using a separating funnel, standing for layering, removing the water phase, and reserving the oil phase to obtain colorless oily liquid. The reaction product was distilled under reduced pressure to remove n-heptane and unreacted reaction materials in the reaction system. After the reduced pressure distillation is finished, brown oily liquid with certain viscosity is prepared, namely the ester compound of the invention, and the theoretical structure of the ester compound is shown as the following formula:
Figure BDA0002746174020000081
the element composition is C22H30O2The theoretical proportion (%) of each element is: c, 80.98; h, 9.20; o, 9.82; the elemental analysis of the obtained ester compound showed that (percent): c, 81.04; h, 9.11; o: 9.85. it can be seen that the structural analysis of the obtained ester compound is accurate.
Example 2
In a 1L round-bottom flask were added 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane and the mixture was heated to 70 ℃ with stirring. After naphthalene is completely dissolved, 2.33g of Y-type molecular sieve is added into the mixture, the mixture is continuously stirred and heated to 90 ℃, nitrogen is filled at the same time, good reflux of n-heptane is kept, and the reaction is carried out for 3 hours at 150 ℃. And when the reaction liquid is cooled to about 50 ℃, closing the nitrogen protection, and removing the solid catalyst by vacuum filtration to obtain dark brown oily liquid. The reaction product was distilled under reduced pressure to remove n-heptane and unreacted reaction materials in the reaction system. After the reduced pressure distillation is finished, brown oily liquid with certain viscosity is prepared, namely the ester compound of the invention.
Example 3
A1L round-bottom flask was charged with 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane, and heated to 70 ℃ with stirring. After naphthalene is completely dissolved, adding 2.33g of trifluoromethanesulfonic acid into the mixture, continuing stirring and heating to 90 ℃, simultaneously introducing nitrogen, keeping n-heptane well refluxing, reacting at 130 ℃ for 3 hours, then cooling to 50 ℃, closing nitrogen protection, and removing trifluoromethanesulfonic acid by vacuum filtration to obtain dark brown oily liquid. Respectively carrying out alkali washing and water washing 3 times by using 0.1mol/L sodium hydroxide solution and deionized water, separating a water phase and an oil phase by using a separating funnel, standing for layering, removing the water phase, and reserving the oil phase to obtain colorless oily liquid. And distilling the reaction product under reduced pressure to remove the solvent and unreacted reaction raw materials in the reaction system. After the reduced pressure distillation is finished, cooling is carried out under the protection of nitrogen, and a tawny oily liquid, namely the ester compound is obtained.
Example 4
A1L round-bottomed flask was charged with 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane and heated to 70 ℃ with stirring. After naphthalene is completely dissolved, dropwise adding 2.5ml of boron trifluoride diethyl etherate into the mixture, continuously stirring and heating to 90 ℃, simultaneously introducing nitrogen, keeping n-heptane to be in good reflux, reacting for 3 hours at 130 ℃, then cooling to 50 ℃, and closing the nitrogen protection to obtain colorless oily liquid. Respectively carrying out alkali washing and water washing 3 times by using 0.1mol/L sodium hydroxide solution and deionized water, separating a water phase and an oil phase by using a separating funnel, standing for layering, removing the water phase, and reserving the oil phase to obtain light yellow oily liquid. And distilling the reaction product under reduced pressure to remove the solvent and unreacted reaction raw materials in the reaction system. After the reduced pressure distillation is finished, cooling is carried out under the protection of nitrogen, and a tawny oily liquid, namely the ester compound is obtained.
Example 5
A1L round-bottom flask was charged with 0.375mol of 1-methylnaphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane, and heated to 70 ℃ with stirring. After naphthalene is completely dissolved, adding 2.33g of Y-type molecular sieve into the mixture, continuously stirring and heating to 90 ℃, simultaneously introducing nitrogen, keeping n-heptane to be well refluxed, reacting for 3 hours at 150 ℃, then cooling to 50 ℃, closing nitrogen protection, and removing the molecular sieve catalyst by vacuum filtration to obtain dark brown oily liquid. And distilling the reaction product under reduced pressure to remove the solvent and unreacted reaction raw materials in the reaction system. After the reduced pressure distillation is finished, cooling is carried out under the protection of nitrogen, and a tawny oily liquid, namely the ester compound is obtained.
Example 6
A1L round-bottom flask was charged with 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane, and heated to 70 ℃ with stirring. After naphthalene is completely dissolved, adding 2.33g of Y-type molecular sieve into the mixture, continuously stirring and heating to 90 ℃, simultaneously introducing nitrogen, keeping n-heptane to be in good reflux, reacting for 3 hours at 180 ℃, then cooling to 50 ℃, closing nitrogen protection, and removing the molecular sieve catalyst by vacuum filtration to obtain dark brown oily liquid. And distilling the reaction product under reduced pressure to remove the solvent and unreacted reaction raw materials in the reaction system. And after reduced pressure distillation, cooling under the protection of nitrogen to obtain a brown oily liquid, namely the ester compound.
Example 7
A1L round-bottomed flask was charged with 0.375mol of refined naphthalene, 0.75mol of methyl 10-undecenoate and 50ml of n-heptane and heated to 70 ℃ with stirring. After naphthalene is completely dissolved, adding 2.33g of Y-type molecular sieve into the mixture, continuously stirring and heating to 90 ℃, simultaneously introducing nitrogen, keeping n-heptane to be well refluxed, reacting for 1 hour at 150 ℃, then cooling to 50 ℃, closing nitrogen protection, and removing the molecular sieve catalyst by vacuum filtration to obtain dark brown oily liquid. And distilling the reaction product under reduced pressure to remove the solvent and unreacted reaction raw materials in the reaction system. After the reduced pressure distillation is finished, cooling is carried out under the protection of nitrogen, and a tawny oily liquid, namely the ester compound is obtained.
Example 8
Adding an additive T501 into the ester compound of example 1, the ester compound of example 5, alkyl naphthalene and mineral oil S6 respectively to prepare uniform solutions with the mass concentration of T501 of 0.5%, and performing DSC oxidation resistance tests on the solution samples respectively, wherein the test results are shown in Table 1, the test instruments are TA5000 DSC instruments of the American TA company, and the test conditions are as follows: 190 ℃, oxygen pressure of 0.5MPa and heating speed of 10 ℃/min.
TABLE 1
Figure BDA0002746174020000101
The comparison shows that the ester compound can obviously improve the oxidation induction period as the base oil, has better oxidation resistance than alkyl naphthalene and mineral oil, and is the base oil with excellent oxidation resistance.
Example 9
Adding an additive T511 into the ester compound of example 1, the ester compound of example 5, the alkyl naphthalene and the mineral oil S6 respectively to prepare uniform solutions with the mass concentration of T511 of 0.5%, and performing DSC oxidation resistance tests on the solution samples respectively, wherein the test results are shown in Table 2, the test instruments are TA5000 DSC instruments of the American TA company, and the test conditions are as follows: 190 ℃, oxygen pressure of 0.5MPa and heating speed of 10 ℃/min.
TABLE 2
Figure BDA0002746174020000111
The comparison shows that the ester compound can obviously improve the oxidation induction period as the base oil, has better oxidation resistance than alkyl naphthalene and mineral oil, and is the base oil with excellent oxidation resistance.
The above embodiments are only used to illustrate the technical solutions of the embodiments of the present disclosure, and not to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, it will be understood by those of ordinary skill in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some technical features may be equivalently replaced; and such modifications or substitutions do not depart from the spirit and scope of the corresponding technical solutions of the embodiments of the present disclosure.

Claims (10)

1. The structure of the ester compound is shown as the formula (I):
Figure FDA0002746174010000011
in the formula (I), Ar ring group is C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthracenyl);
n is an integer of 1 to 20 (preferably an integer of 1 to 15, more preferably an integer of 1 to 10, and further preferably an integer of 1 to 6);
n R groups are bonded to the Ar ring group;
n R groups are each independently selected from the group of formula (II), C1~30Is preferably independently selected from the group represented by the formula (II), C1~20More preferably, each of the straight-chain or branched alkyl groups and H is independently selected from the group represented by the formula (II), C1~10H) and at least one R group is selected from the group represented by formula (II);
Figure FDA0002746174010000012
in the formula (II), m is an integer of 1 to 10 (preferably an integer of 1 to 5, more preferably 1, 2 or 3); r1The radicals being selected from C1~30Is preferably selected from C1~20More preferably selected from C1~10Linear or branched alkyl groups of (a); m number of R2Each independently selected from C1~30Alkylene group of (2), a single bond (preferably selected from C)1~20Is more preferably selected from C1~10Linear or branched alkylene, single bond, with
Figure FDA0002746174010000013
Bonded R2The radicals are preferably selected from C1~10Linear or branched alkylene groups of (a); r3The radicals being selected from C1~30Is preferably selected from C, H1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H);
m a 'groups are each independently selected from-CH ═ CH-, ethylene-, a group represented by formula (III), a group represented by formula (IV), a group represented by formula (V) and a group represented by formula (VI), and at least one a' group present in formula (II) is selected from a group represented by formula (III) or a group represented by formula (IV), the group represented by formula (III) or formula (IV) is bonded to the Ar ring group in formula (I), and represents a bonding end at which the group represented by formula (III) or formula (IV) is bonded to the Ar ring group in formula (I);
Figure FDA0002746174010000021
in the group represented by the formula (III), the group represented by the formula (IV), the group represented by the formula (V) and the group represented by the formula (VI), each R4Each independently selected from C1~30Is preferably selected from C, H1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H); ar ring radical being C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthracenyl).
2. An ester compound according to claim 1, wherein the ester compound comprises one or more of the following compounds in any ratio:
Figure FDA0002746174010000022
3. a process for producing an ester compound, which comprises the step of reacting a compound represented by the formula (alpha) with a compound represented by the formula (beta),
Figure FDA0002746174010000031
in the formula (. alpha.), m is an integer of 1 to 10 (preferably an integer of 1 to 5, more preferably 1, 2 or 3); r is1The radicals being selected from C1~30Is preferably selected from C1~20More preferably selected from C1~10Linear or branched alkyl groups of (a); m R2Each independently selected from C1~30Alkylene group of (2), a single bond (preferably selected from C)1~20Linear chain of (2)Or a branched alkylene group, a single bond, more preferably C1~10A straight or branched alkylene group of (A), a single bond, and
Figure FDA0002746174010000032
bonded R2The radicals are preferably selected from C1~10Linear or branched alkylene groups of (a); r3The radicals being selected from C1~30Is preferably selected from C, H1~20Is selected from the group consisting of H, and C1~10Straight or branched alkyl of (a), H);
in the formula (. beta.), Ar ring group is C6~20Aryl (preferably C)6~15Aryl, more preferably C6~10Aryl, more preferably phenyl, naphthyl, anthracenyl); n' is an integer of 1 to 19 (preferably an integer of 1 to 14, more preferably an integer of 1 to 9, and further preferably an integer of 1 to 5);
n 'R' groups are bonded to the Ar ring group;
n 'R' radicals are each independently selected from C1~30Is preferably independently selected from C1~20More preferably each is independently selected from C1~10Straight or branched alkyl, H).
4. A method according to claim 3, wherein the compound of formula (α) is selected from one or more of the following compounds: octenoic acid, decenoic acid, undecenoic acid, dodecenoic acid, decatetraenoic acid, hexadecenoic acid, oleic acid, linoleic acid, linolenic acid, eicosenoic acid; and/or, the compound shown in the formula (beta) is selected from one or more of the following compounds: benzene, naphthalene, anthracene, methylnaphthalene, ethylnaphthalene, n-propylnaphthalene, 2-isopropylnaphthalene.
5. The method according to claim 3, wherein the mass ratio between the compound represented by the formula (α) and the compound represented by the formula (β) is 1: 0.1-1 (preferably 1: 0.2-1), and the reaction temperature is 60-200 deg.C (preferably 90-180 deg.C).
6. A process according to claim 3, characterized in that the compound of formula (α) is reacted with the compound of formula (β) in the presence of an inert gas.
7. A process according to claim 3, characterized in that a catalyst, preferably an acidic catalyst, is added to the reaction of the compound of formula (α) with the compound of formula (β).
8. The process of claim 7 wherein the catalyst is selected from the group consisting of Lewis acids, or mixtures thereof,
Figure FDA0002746174010000041
One or more of acid, solid acid, acidic ionic liquid and its supported catalyst, the carrier of the supported catalyst can be molecular sieve, alumina, zeolite, graphite, carbon black, resin (the acidic catalyst is preferably one or more of aluminum trichloride, stannic chloride, boron trifluoride, sulfuric acid, hydrofluoric acid, phosphoric acid, Y-type molecular sieve, M-type molecular sieve, beta zeolite, mordenite, phosphotungstic acid, silicon aluminum fluoride, perfluoroalkane sulfonic acid and its supported catalyst).
9. Use of the ester compound of claim 1 or 2 or the ester compound prepared according to the method of any one of claims 3 to 8 as a lubricating base oil.
10. A lubricating oil composition comprising the ester compound of claim 1 or 2 or the ester compound produced by the method of any one of claims 3 to 8 and a lubricating oil additive.
CN202011167141.4A 2020-10-28 2020-10-28 Ester compound and preparation method and application thereof Pending CN114507138A (en)

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CN104370729A (en) * 2014-11-13 2015-02-25 大连东方创新科技有限公司 Synthesis method and system for aryl alkyl carboxylic acid (methyl ester)
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US20190100710A1 (en) * 2017-09-29 2019-04-04 Exxonmobil Chemical Patents Inc. Ester Compounds, Lubricating Oil Compositions Containing Same and Processes for Making Same
CN111032613A (en) * 2017-08-28 2020-04-17 埃克森美孚化学专利公司 Ester compound, lubricating oil composition containing the same, and process for producing the same
CN111088091A (en) * 2018-10-23 2020-05-01 中国石油化工股份有限公司 Gasoline engine oil composition and preparation method thereof
CN111088092A (en) * 2018-10-23 2020-05-01 中国石油化工股份有限公司 Heavy-duty diesel engine oil composition and preparation method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104326906A (en) * 2014-09-12 2015-02-04 大连东方创新科技有限公司 Aryl alkyl carboxylic monoester and preparation method and application thereof
CN104370729A (en) * 2014-11-13 2015-02-25 大连东方创新科技有限公司 Synthesis method and system for aryl alkyl carboxylic acid (methyl ester)
WO2017116900A1 (en) * 2015-12-28 2017-07-06 Exxonmobil Research And Engineering Company High viscosity index monomethyl ester lubricating oil base stocks and methods of making and use thereof
CN111032613A (en) * 2017-08-28 2020-04-17 埃克森美孚化学专利公司 Ester compound, lubricating oil composition containing the same, and process for producing the same
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