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CN115960649B - Lubricating grease and preparation method thereof - Google Patents

Lubricating grease and preparation method thereof Download PDF

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Publication number
CN115960649B
CN115960649B CN202111179592.4A CN202111179592A CN115960649B CN 115960649 B CN115960649 B CN 115960649B CN 202111179592 A CN202111179592 A CN 202111179592A CN 115960649 B CN115960649 B CN 115960649B
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grease
reaction
peroxide
group
compound
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CN115960649A (en
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庄敏阳
李朝宇
韩天昊
陈晓伟
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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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Abstract

The invention provides lubricating grease, which comprises a thickening agent, an additive and a main amount of lubricating base oil, wherein the additive comprises an organoboron compound and an antirust agent, and the structure of the organoboron compound is shown as a formula (I):

Description

Lubricating grease and preparation method thereof
Technical Field
The invention relates to lubricating grease, in particular to lithium-based lubricating grease and a preparation method thereof.
Background
Grease is a necessary working medium in the normal operation of mechanical equipment and the material manufacturing process, and the demand of the grease is also increasing along with the high-speed development of industry. Lithium-based lubricating grease is a product with the largest worldwide output and the widest application field, which is most valued by the lubricating grease industry of various countries, and plays a very important role in the current industrial lubrication.
In recent years, with the progress of industrial technology, the working condition of the application part of the lubricating grease is more severe, which puts higher requirements on the lubricating grease additive, and with the restriction of environmental protection, new demands of low ash content and low phosphorus content are also put forward. The boron-containing lubricating material has the characteristics of extreme pressure wear resistance, high temperature oxidation resistance, corrosion resistance, rust resistance, good sealing performance, environmental suitability, no toxicity, no odor and the like; the nitrogen-containing lubricating material has the characteristics of no ash, high electronegativity, small atomic radius, easy formation of hydrogen bonds between molecules adsorbed on the metal surface, improvement of oil film strength and the like; and both the two lubricating materials have the advantages of multifunction, designable molecular structure, combinable active elements and the like. Therefore, research on nitrogen-containing organoboron lubricating materials has attracted considerable attention in the field of modern friction and lubrication. The development of grease products associated therewith is also a direction of development by those skilled in the art.
Disclosure of Invention
The invention provides lubricating grease and a preparation method thereof.
The lubricating grease comprises a thickening agent, an additive and a main amount of lubricating base oil, wherein the additive comprises an organoboron compound and an antirust agent, and the structure of the organoboron compound is shown as a formula (I):
In formula (I), a repeating units L and b boron-containing groups are present, a being an integer between 1 and 10 (preferably an integer between 1 and 5), b being an integer between 1 and 5 (preferably an integer between 1 and 3), a being identical or different from each other and each independently selected from groups of formula (II);
In formula (II), HO is bonded to the benzene ring (HO is preferably located in the meta position of the chain on the benzene ring where R 1 is located); y R groups are bonded to the benzene ring; y is selected from integers between 0 and 4 (preferably integers between 1 and 3); the R groups are each independently selected from H and C 1-20 straight or branched alkyl (preferably each independently selected from H and C 1-4 straight or branched alkyl, more preferably t-butyl); n is an integer between 1 and 10 (preferably an integer between 1 and 3); r 1 is each independently selected from a single bond and a C 1-20 linear or branched alkylene (preferably selected from a single bond and a C 1-4 linear or branched alkylene); r 2 in the n repeating units, equal to or different from each other, are each independently selected from a single bond and a C 1-20 linear or branched alkylene group (preferably each independently selected from a single bond and a C 1-4 linear or branched alkylene group); r 3 is selected from H and C 1-20 linear or branched alkyl (preferably from H and C 1-4 linear or branched alkyl); the A groups in the n repeating units are identical or different from each other and are each independently selected from single bonds, A group represented by the formula (III) and a group represented by the formula (IV),
The R 4 groups are each independently selected from H and C 1-20 linear or branched alkyl (preferably from H and C 1-4 linear or branched alkyl);
m is an integer between 0 and 10 (preferably an integer between 1 and 5);
The R 5 groups are each independently selected from C 1-20 linear or branched alkyl groups of valency 3 (preferably each independently selected from C 1-4 linear or branched alkyl groups of valency 3);
Each G 2 group is independently selected from the group consisting of a binding end bonded to a G 4 group present in other L groups than the L group in which it is located, C 1-10 straight or branched alkyl, -R 6G3, H; each G 3 group is independently selected from-OG 1、C1-10 linear or branched alkyl, H (preferably each is independently selected from-OG 1、C1-4 linear or branched alkyl, OH, H);
The R 6 groups are selected from C 1-20 linear or branched alkylene groups (preferably each independently selected from C 1-4 linear or branched alkylene groups);
The G 1 group is selected from the group consisting of a binding end bonded to the boron-containing group, H;
the G 4 group is selected from the binding end, H, bonded to the G 2 group present in the other L groups than the L group in which it is located;
of the a groups, at least one A group is selected from the group represented by formula (III), and at least one G 1 group is selected from the binding end bonded to the boron element in the boron-containing group;
Each a ' group of b said boron-containing groups is independently selected from the group consisting of a binding end bonded to a G 1 group present in the L group, a group of formula (V), OH, -OR ', said R ' groups being C 2-20 linear OR branched alkyl groups (preferably C 1-4 linear OR branched alkyl groups);
in formula (V), m is an integer between 0 and 10 (preferably an integer between 1 and 5);
The R 0 groups are each independently selected from C 1-10 linear or branched alkyl, -R 6G5, H (preferably each independently selected from C 1-4 linear or branched alkyl, -R 6G5, H);
The R 5 groups are each independently selected from C 1-20 linear or branched alkyl groups of valency 3 (preferably each independently selected from C 1-4 linear or branched alkyl groups of valency 3);
The group G 6 is selected from the group consisting of-R 6G5、C1-4 straight or branched alkyl, H;
The R 6 groups are selected from C 1-20 linear or branched alkylene groups (preferably each independently selected from C 1-4 linear or branched alkylene groups);
Each G 5 group is independently selected from-OG 1、C1-4 linear or branched alkyl, OH, H, wherein the G 1 group is selected from the group consisting of a binding end bonded to the boron element in the boron-containing group, C 1-4 linear or branched alkyl, H;
In the group represented by the formula (V), at least one G 1 group is selected from the binding end bonded to the boron element in the boron-containing group;
Of the b boron-containing groups, at least one a' group is present selected from the binding end to which the G 1 group present in the L group is bonded;
Each group in the organoboron compound conforms to the bond formation rules.
According to the invention, the binding end of the two of formula (III) or (IV) bound to formula (II) may be bound to the group of formula (II) in any way, for example in one direction or in the opposite direction.
Examples of the organoboron compound which may be cited according to the present invention include one or more of the following structural compounds:
Wherein the R group is a linear or branched alkyl group of C 2-C20.
According to the present invention, the method for preparing an organoboron compound comprises the steps of:
(1) Reacting a compound represented by formula (X) with a peroxide;
In formula (X), HO is bonded to the benzene ring (HO is preferably located in the meta position of the chain on the benzene ring where R 1 is located); y R groups are bonded to the benzene ring; y is selected from integers between 0 and 4 (preferably integers between 1 and 3); the R groups are each independently selected from H and C 1-20 linear or branched alkyl (preferably each independently selected from H and C 1-4 linear or branched alkyl, more preferably selected from t-butyl); n is an integer between 1 and 10 (preferably an integer between 1 and 3); r 1 is each independently selected from a single bond and a C 1-20 linear or branched alkylene (preferably selected from a single bond and a C 1-4 linear or branched alkylene); r 2 in the n repeating units, equal to or different from each other, are each independently selected from a single bond and a C 1-20 linear or branched alkylene group (preferably each independently selected from a single bond and a C 1-4 linear or branched alkylene group); r 3 is selected from H and C 1-20 linear or branched alkyl (preferably from H and C 1-4 linear or branched alkyl); a' in n repeating units, which are identical or different from each other, are each independently selected from the group consisting of single bonds, Wherein each of said R 4 groups is independently selected from H and C 1-20 straight or branched alkyl (preferably from H and C 1-4 straight or branched alkyl); in the formula (X), at least one A' is
(2) Reacting the reaction product of step (1) with a compound represented by formula (Y);
in formula (Y), m is an integer between 0 and 10 (preferably an integer between 1 and 5);
The R 0' groups are each independently selected from C 1-10 straight or branched alkyl, -R 6 OH, H (preferably each independently selected from C 1-4 straight or branched alkyl, -R 6 OH, H); the R 5 groups are each independently selected from C 1-20 linear or branched alkyl groups of valency 3 (preferably each independently selected from C 1-4 linear or branched alkyl groups of valency 3); each G 5' group is independently selected from C 1-4 straight or branched alkyl, OH, H; the G 6' group is selected from C 1-10 straight-chain or branched-chain alkyl, -R 6 OH and H; the R 6 groups are each independently selected from C 1-20 linear or branched alkylene (preferably each independently selected from C 1-4 linear or branched alkylene);
In formula (Y), at least one G 5 ' group is selected from OH or at least one G 6 ' group or R 0 ' group is selected from-R 6 OH, and at least one R 0 ' group or G 6 ' group is H;
(3) Reacting the reaction product of step (2) with an inorganic boron compound, and collecting the product.
According to the present invention, in step (1), the compound represented by formula (X) may be selected from cardanol, alkylated cardanol, which may be obtained by reacting cardanol with an alkylating agent, for example, tert-butylated cardanol may be obtained by reacting cardanol with tert-butylchloride.
According to the present invention, in the step (1), the peroxide is preferably one or more of hydrogen peroxide, peroxyformic acid, peroxyacetic acid, peroxysulfonic acid, m-chloroperoxybenzoic acid, t-butyl hydroperoxide, t-butyl peroxyacetate, methyl ethyl ketone peroxide, dibenzoyl peroxide and cyclohexanone peroxide, more preferably one or more of hydrogen peroxide, peroxyformic acid, peroxyacetic acid and peroxysulfonic acid.
According to the present invention, in the step (2), the compound represented by the formula (Y) may be selected from one or more of aliphatic amine, polyene polyamine, one or more hydroxyl-substituted aliphatic amine, one or more hydroxyl-substituted polyene polyamine, and for example, one or more of ethanolamine, diethanolamine, hydroxyethyl ethylenediamine (i.e., N- (2-hydroxyethyl) ethylenediamine), diethylenetriamine, triethylenetetramine, tetraethylenepentamine, and pentaethylenehexamine may be selected.
According to the invention, in step (3), the inorganic boron compound is preferably selected from one or more of boric acid, boric oxide and boric acid half-ester, wherein the boric acid half-ester can be selected from monoalkyl borate and dialkyl borate, and the alkyl is C 2-C20 straight-chain or branched-chain alkyl.
According to the present invention, the equivalent ratio between the compound represented by the formula (X) and the peroxide, the compound represented by the formula (Y), the inorganic boron compound is preferably 1:0.5 to 10:0.5 to 10:0.5 to 5, more preferably 1: 2-3: 2-3: 1 to 2.
According to the present invention, the reaction temperature in step (1) is preferably 0 to 100 ℃, more preferably 20 to 80 ℃; the reaction temperature in the step (2) is preferably 50 to 150 ℃, more preferably 60 to 100 ℃; the reaction temperature in the step (3) is preferably 80 to 200℃and more preferably 110 to 150 ℃.
According to the present invention, the longer the reaction time of step (1), step (2) and step (3), the better, the reaction time of step (1) is preferably 1 to 10 hours, more preferably 3 to 5 hours; the reaction time in the step (2) is preferably 1 to 10 hours, more preferably 2 to 4 hours; the reaction time in the step (3) is preferably 1 to 10 hours, more preferably 3 to 5 hours.
According to the present invention, in the reaction of step (3), a compound represented by formula (Y) may be further added, the equivalent ratio between the compound represented by formula (Y) and the inorganic boron compound preferably being 1:0.5 to 5, more preferably 1:0.8 to 3.
According to the invention, the reaction steps (1), (2) or (3) may be carried out in the presence of a diluent and/or solvent, or may be carried out without a diluent and/or solvent.
According to the invention, the diluent can be one or more of API I, II, III, IV and V base oils, and common commercial products or marks comprise 150SN、200SN、350SN、500SN、650SN、150BS、HVI-100、HVI-150、HVI-200、HVI-350、HVI-400、HVI-500、HVI-150BS、PAO4、PAO6、PAO8、PAO10、 alkylbenzene, alkyl naphthalene and the like.
According to the present invention, the solvent may be selected from C 6-20 aromatic hydrocarbons (such as benzene, toluene, xylene and cumene), C 6-10 alkanes (such as n-hexane, cyclohexane and petroleum ether), solvent gasoline, and the like. These solvents may be used alone or in combination of two or more. The solvent may be distilled off after the reaction is completed, using a means well known to those skilled in the art, for example, under normal pressure or reduced pressure.
According to a particular embodiment of the present invention, the diluent and/or solvent may be added at any stage of the reaction step in an amount conventional in the art, without particular limitation.
According to the invention, it is evident that the reaction step is generally carried out under protection of an inert gas atmosphere. Examples of the inert gas include nitrogen and argon, but are not particularly limited.
According to the present invention, in step (3), an accelerator for promoting completion of the reaction may be added, and common accelerators include water, ethanol, propanol, butanol, ammonia water, etc. If accelerators are added, they can be distilled off after the end of the reaction, using means known to the person skilled in the art, for example under atmospheric or reduced pressure.
According to the present invention, by the aforementioned method for producing an organoboron compound, a single organoboron compound, a mixture of plural organoboron compounds, or a mixture of one or more of the organoboron compounds and the aforementioned diluent (if used) can be produced as a reaction product. These reaction products are all contemplated by the present invention and the differences in their form of presence do not affect the achievement of the effects of the present invention. Accordingly, these reaction products are collectively referred to herein without distinction as organoboron compounds. In view of this, according to the present invention, there is no absolute necessity of further purifying the reaction product, or further separating an organoboron compound of a specific structure from the reaction product. Of course, this purification or isolation is preferred for further enhancement of the intended effect of the invention, but is not required for the invention. The purification or separation method may be, for example, a method of purifying or separating the reaction product by column chromatography or preparative chromatography.
The organic boron compound has excellent oxidation resistance, wear resistance and antifriction performance.
According to the invention, the rust inhibitor is preferably one or more of sulfonate, naphthenate, imidazoline compound, carboxylic acid and carboxylate, more preferably one or more of petroleum sulfonate, synthetic sulfonate, naphthenate and imidazoline compound, for example, one or more of barium petroleum sulfonate, barium dinonyl naphthalene sulfonate, zinc naphthenate and heptadecenyl imidazoline alkenyl succinate, and common commercial products include T701, T705, T704 and T703, etc.
According to the invention, the additive comprises a mixture of an organoboron compound and an anti-rust agent, wherein the mass ratio between the organoboron compound and the anti-rust agent is 1:0.05 to 20, more preferably 1:0.5 to 5.
According to the present invention, the thickener is preferably one or more selected from lithium-based thickeners, calcium-based thickeners, aluminum-based thickeners, anhydrous calcium-based thickeners, sodium-based thickeners and barium-based thickeners, more preferably lithium-based thickeners.
According to the present invention, the lithium-based thickener is preferably obtained by saponification of a fatty acid with lithium hydroxide. The temperature of the saponification reaction is preferably 60 to 180 ℃, more preferably 70 to 160 ℃. The saponification reaction time is preferably 30 to 300 minutes, more preferably 50 to 240 minutes. The fatty acid is preferably selected from the group consisting of C 12~C20 fatty acids and/or C 12~C20 hydroxy fatty acids, for example, one or more of lauric acid, myristic acid, palmitic acid, oleic acid, stearic acid and 12-hydroxystearic acid, more preferably 12-hydroxystearic acid and/or stearic acid. Water is preferably added during the saponification reaction. The water can directly participate in the saponification reaction, or can participate in the saponification reaction after being mixed with the lithium hydroxide into a solution. Part of the lubricating base oil may be added during the saponification reaction. The lithium-based thickener may be a lithium-based thickener that includes a portion of a lubricating base oil.
According to the present invention, the lubricating base oil is preferably one or more of mineral oil, vegetable oil and synthetic oil. The mineral oil may be one or more of a paraffinic base oil, an intermediate base oil, and a naphthenic base oil; the vegetable oil can be one or more of castor oil, rapeseed oil, peanut oil and soybean oil; the synthetic oil may be one or more of poly alpha-olefin oil, ester oil, fluorine oil and silicone oil. The lubricating base oil is preferably a lubricating base oil having a kinematic viscosity of 5 to 60mm 2/s at 100 ℃, and most preferably a lubricating base oil having a kinematic viscosity of 10 to 30mm 2/s at 100 ℃.
According to the present invention, preferably, the additive accounts for 1% to 10% of the grease; the thickening agent accounts for 4% -30% of the lubricating grease; the lubricating base oil accounts for 65% -95% of the lubricating grease; more preferably, the additive accounts for 2% -8% of the grease; the thickening agent accounts for 8% -20% of the lubricating grease; the lubricating base oil accounts for 75% -90% of the lubricating grease.
The preparation method of the lubricating grease provided by the invention comprises the following steps: the thickener and part of lubricating base oil are refined at a high temperature of 190-220 ℃, cooled, added with the additive and the rest of lubricating base oil and ground into grease. The refining time is preferably 1 to 25 minutes.
The lubricating grease disclosed by the invention has excellent oxidation resistance and wear resistance, good colloid stability and excellent mechanical stability, and can be used for severe working conditions such as high temperature, high speed, high load, multiple water and the like.
Detailed Description
In this specification, the term "single bond" is sometimes used in the definition of a group. By "single bond" is meant that the group is absent. For example, assume the structural formula-CH 2-A-CH3, wherein the group a is defined as selected from single bonds and methyl. In view of this, if A is a single bond, this means that the group A is absent, in which case the formula is correspondingly reduced to-CH 2-CH3.
In the context of the present specification, the expression "number +valence +group" or the like means a group obtained by removing the number of hydrogen atoms represented by the number from a basic structure (such as a chain, a ring, or a combination thereof, etc.) to which the group corresponds, preferably a group obtained by removing the number of hydrogen atoms represented by the number from carbon atoms (preferably saturated carbon atoms and/or non-identical carbon atoms) contained in the structure. For example, "3-valent linear or branched alkyl group" refers to a group obtained by removing 3 hydrogen atoms from a linear or branched alkane (i.e., the basic chain to which the linear or branched alkyl group corresponds).
The invention is further illustrated by the following examples, which are not to be construed as limiting the invention.
The main raw materials used are as follows:
cardanol, shanghai Material competition technology Co., ltd, industrial products
Zinc chloride, concentrated sulfuric acid, hydrogen peroxide (30%), formic acid, boric acid, diethanolamine, diethylenetriamine, N- (2-hydroxyethyl) ethylenediamine, tert-butyl chloride, all purchased from national pharmaceutical group chemical reagent company, analytical grade T701, barium petroleum sulfonate, new Dou Dan oil additive plant in Chengdu, industrial products
T705, barium dinonyl naphthalene sulfonate, suzhou specialty oil works, industrial products
EXAMPLE 1 preparation of tert-butylated epoxy Cardanol
100 G of cardanol, 8 g of formic acid, 0.3 g of sulfuric acid and 200g of hydrogen peroxide are taken and added into a three-neck flask with a mechanical stirring and reflux condenser and temperature control, and stirring and heating are started. The reaction temperature was maintained at 70℃and the reaction was carried out for 3 hours. And cooling after the reaction is finished to obtain brownish red transparent liquid. Filtering the reaction product, performing alkali washing with 5% KOH solution, washing with distilled water to neutrality, and distilling the organic phase under reduced pressure at 100Pa and 150 ℃ for 1h to remove water and unreacted raw materials to obtain the orange-red transparent liquid epoxidized cardanol.
35 G of epoxidized cardanol is dissolved in 100ml of acetone, the dissolved cardanol is put into a 250ml three-neck reaction flask, 0.9 g of zinc chloride catalyst is added, and stirring and heating are started. The reaction temperature was maintained at 60℃and 9.5 g of t-butyl chloride was slowly added dropwise to the reaction flask, followed by further reaction for 3 hours after completion of the dropwise addition. And cooling after the reaction is finished to obtain brownish red transparent liquid. Filtering the reaction product, performing alkali washing with 5% KOH solution, washing with distilled water to neutrality, and performing reduced pressure distillation at 1000Pa and 120 ℃ for 1h to remove solvent, water and unreacted raw materials to obtain brownish red viscous liquid tert-butyl epoxy cardanol.
An example reaction scheme of the above reaction is shown below.
Example 2
22 G of t-butylated hydroxycardanol prepared in example 1,5 g of N- (2-hydroxyethyl) ethylenediamine and 90 g of toluene were put into a 250mL three-necked flask, and the mixture was heated with stirring to react at 90℃for 3 hours. After the reaction, the solvent and unreacted raw materials are removed by reduced pressure distillation for 1h to obtain dark brown red viscous liquid tert-butyl amino cardanol, then 3 g of boric acid, 10 g of N- (2-hydroxyethyl) ethylenediamine and 90 g of cyclohexane are added into a reaction vessel, stirring, heating, dehydrating, reacting for 3h at 120 ℃, and finally filtering, evaporating the solvent and unreacted N- (2-hydroxyethyl) ethylenediamine to obtain an organoboron compound W-01.
An exemplary reaction scheme is shown below, wherein R is H.
The product prepared in example 2 was subjected to infrared spectroscopic analysis, and the analysis results are shown in table 1.
TABLE 1 Infrared analysis results of the products
The characteristic peaks such as C-OH stretching vibration peak, C-NH stretching vibration peak, benzene ring skeleton stretching vibration peak, N-C stretching vibration peak, O-C stretching vibration peak and B-O stretching vibration peak are shown in Table 1, and the synthesized product can be indicated as the target compound.
Example 3
36G of the tert-butylated hydroxycardanol prepared in example 1, 10g of diethanolamine and 90g of toluene were charged into a 250mL three-necked flask, heated with stirring and reacted at 100℃for 4 hours. After the reaction is finished, the solvent and unreacted raw materials are removed through reduced pressure distillation for 1h, dark brown red viscous liquid tertiary butyl amino cardanol is obtained, then 6g boric acid, 20g diethanolamine and 90g cyclohexane are added into a reaction vessel, stirring and heating are carried out, water is removed, the reaction is carried out for 4h at 150 ℃, and finally the solvent and unreacted diethanolamine are filtered and distilled off, thus obtaining the organoboron compound W-02.
Example 4
21.5 G of the tert-butylated hydroxycardanol prepared in example 1, 6 g of diethylenetriamine and 90 g of toluene were charged into a 250mL three-necked flask and heated with stirring to react at 95℃for 2 hours. After the reaction, distilling under reduced pressure for 1h, removing the solvent and unreacted raw materials to obtain dark brown red viscous liquid tert-butyl amino cardanol, adding 6 g boric acid, 8g cetyl alcohol, 10.5 g diethylenetriamine and 90 g cyclohexane into a reaction vessel, stirring, heating, removing water, reacting at 145 ℃ for 5h, and finally filtering, evaporating to remove the solvent and unreacted diethylenetriamine to prepare the organoboron compound W-03.
Example I-1
The raw material components are as follows: 500SN 1073 g (viscosity at 100 ℃ C. 11mm 2/s); 10.41 g of anhydrous lithium hydroxide; 129.62 g of 12-hydroxystearic acid; 10.94 g of barium petroleum sulfonate; w-01 organoboron compound 10.01 g.
Firstly adding 605 g of 500SN base oil and 129.62 g of 12-hydroxystearic acid into a fat preparation kettle, uniformly mixing, adding 99.72 g of lithium hydroxide aqueous solution (containing 10.41 g of lithium hydroxide and 89.31 g of water) when the temperature is raised to 80 ℃ for saponification reaction for 120min, heating to 150 ℃ for dehydration reaction, continuously heating to 200 ℃ for high-temperature refining for 10min after dehydration, adding 468 g of 500SN base oil, cooling to 100 ℃, adding 10.94 g of barium petroleum sulfonate and 10.01 g of W-01 organic boron compound, uniformly stirring, and grinding into fat by a three-roller machine.
Example I-2
The raw material components are as follows: 500SN 998 g (viscosity at 100 ℃ C. 11mm 2/s); 11.24 g of anhydrous lithium hydroxide; 146.31 g of 12-hydroxystearic acid; barium dinonyl naphthalene sulfonate 11 g, W-01 organoboron compound 10 g.
Firstly, adding 503 g of 500SN base oil and 146.31 g of 12-hydroxystearic acid into a fat preparation kettle, uniformly mixing, adding 101.25 g of lithium hydroxide aqueous solution (containing 11.24 g of lithium hydroxide and 90.01 g of water) for saponification reaction for 120min when the temperature is raised to 80 ℃, raising the temperature to 150 ℃ for dehydration reaction, and continuously raising the temperature to 200 ℃ for high-temperature refining for 10min after dehydration; 495 g of 500SN base oil is added, the temperature is reduced to 100 ℃,11 g of barium dinonylnaphthalene sulfonate and 10g of W-01 organic boron compound are added, the mixture is stirred uniformly, and the mixture is ground into grease by a three-roller machine.
Example I-3
The raw material components are as follows: PAO10 808 g (viscosity 10mm 2/s at 100 ℃); 6.76 g of lithium hydroxide; 80.27 g of 12-hydroxystearic acid; 7 g of barium petroleum sulfonate; w-02 organoboron compound 8.6 g.
Adding 421 g of PAO10 base oil and 80.27 g of 12-hydroxystearic acid into a lipid preparation kettle, uniformly mixing, adding 66.93 g of lithium hydroxide aqueous solution (containing 6.76 g of lithium hydroxide and 60.17 g of water) when the temperature is raised to 80 ℃ for saponification reaction for 120min; heating to 150 ℃ for dehydration reaction, and continuously heating to 210 ℃ for refining for 10min after dehydration; 387 g of PAO10 base oil is added, the temperature is reduced to 100 ℃, 7g of barium petroleum sulfonate and 8.6 g of W-02 organic boron compound are added, the mixture is stirred uniformly, and the mixture is ground into grease by a three-roller machine.
Example I-4
The raw material components are as follows: PAO4 796 g (viscosity at 100 ℃ C. 3.9mm 2/s); 5.87 g of lithium hydroxide; 71.12 g of 12-hydroxystearic acid; 9 g of barium petroleum sulfonate and 8 g of W-03 organic boron compound.
Adding 502 g of PAO4 base oil and 71.12 g of 12-hydroxystearic acid into a fat preparation kettle, uniformly mixing, adding 55.97 g of lithium hydroxide aqueous solution (containing 5.87 g of lithium hydroxide and 50.10 g of water) when the temperature is raised to 80 ℃ for saponification reaction for 120min, heating to 130 ℃ for dehydration reaction, continuously heating to 200 ℃ for high-temperature refining for 10min after dehydration, adding 294 g of PAO4 base oil, cooling to 110 ℃, adding 9g of barium petroleum sulfonate and 8g of W-03 organic boron compound, uniformly stirring, and grinding into fat by a three-roller machine.
Comparative example D-1
The raw material components are as follows: 500SN 1068 g (viscosity at 100 ℃ C. 11mm 2/s); 10.27 g of lithium hydroxide; 128.3 grams of 12-hydroxystearic acid; 10.82 g of barium petroleum sulfonate.
Firstly, 612 g of 500SN base oil and 128.3 g of 12-hydroxystearic acid are added into a fat preparation kettle, uniformly mixed, 92.67 g of lithium hydroxide aqueous solution (containing 10.27 g of lithium hydroxide and 82.4 g of water) is added when the temperature is raised to 80 ℃ for saponification reaction for 120min, the temperature is raised to 150 ℃ for dehydration reaction, the temperature is continuously raised to 200 ℃ for high-temperature refining for 10min after dehydration, 456 g of 500SN base oil is added, the temperature is lowered to 100 ℃, 10.82 g of barium petroleum sulfonate is added, uniformly stirred, and the mixture is ground into fat by a three-roll machine.
The properties of the grease obtained were evaluated, and the evaluation items, evaluation methods and evaluation results are shown in Table 2.
Table 2 grease performance assessment

Claims (8)

1. A grease comprising a thickener, an additive and a major amount of a lubricating base oil, wherein the additive comprises an organoboron compound comprising one or more of the following structural compounds and a rust inhibitor:
Wherein R groups are H;
the antirust agent is one or more selected from sulfonate, naphthenate, imidazoline compounds, carboxylic acid and carboxylate; the thickener is one or more selected from lithium-based thickener, calcium-based thickener, aluminum-based thickener, sodium-based thickener and barium-based thickener; the lubricating base oil is selected from one or more of mineral oil, vegetable oil and synthetic oil;
The additive accounts for 1% -10% of the lubricating grease; the thickening agent accounts for 4% -30% of the lubricating grease; the lubricating base oil accounts for 65% -95% of the lubricating grease; the mass ratio of the organoboron compound to the antirust agent in the additive is 1:0.05 to 20.
2. Grease according to claim 1, characterized in that the preparation process of the organoboron compound comprises the following steps:
(1) Enabling cardanol to have an epoxidation reaction with peroxide and then have an alkylation reaction with tertiary butyl chloride;
(2) Reacting the reaction product of step (1) with an amine compound;
The amine compound is selected from one or more of N- (2-hydroxyethyl) ethylenediamine, diethanolamine and diethylenetriamine;
(3) Reacting the reaction product of step (2) with an inorganic boron compound, and collecting the product.
3. A grease according to claim 2, wherein,
In step (1), the peroxide is selected from one or more of hydrogen peroxide, peroxyformic acid, peroxyacetic acid, peroxysulfonic acid, m-chloroperoxybenzoic acid, tert-butyl hydroperoxide, tert-butyl peroxyacetate, methyl ethyl ketone peroxide, dibenzoyl peroxide and cyclohexanone peroxide;
And/or, in the step (3), the inorganic boron compound is selected from one or more of boric acid and boron oxide.
4. Grease according to claim 2, characterized in that the equivalent ratio between cardanol and peroxide, amine compound, inorganic boron compound is 1:0.5 to 10:0.5 to 10:0.5 to 5.
5. Grease according to claim 2, characterized in that the equivalent ratio between cardanol and peroxide, amine compound, inorganic boron compound is 1: 2-3: 2-3: 1 to 2.
6. The grease of claim 2, wherein the reaction temperature of step (2) is 50 to 150 ℃; the reaction temperature of the step (3) is 80-200 ℃.
7. The grease of claim 2, wherein the reaction temperature of step (2) is 60 to 100 ℃; the reaction temperature of the step (3) is 110-150 ℃.
8. A method of preparing the grease of any one of claims 1 to 7, comprising: and (3) refining the thickening agent and part of the lubricating base oil at a high temperature of 190-220 ℃, cooling, adding the additive and the rest of the lubricating base oil, and grinding into grease.
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