The content of the invention
The purpose of the invention is to meet the high request to the antioxygen property of lubricating grease, it is excellent to provide a kind of antioxygen property
Composite aluminum base grease composition and preparation method thereof.
The present inventor has found that the additive in lubricant composition contains structure shown in formula (I) under study for action
Antioxidant:
It can make lubricant composition that there are the excellent performances such as anti-oxidant.
Therefore, to achieve these goals, on the one hand, the present invention provides the composite aluminum base profits that a kind of antioxygen property is excellent
Grease composition, on the basis of the weight of lubricant composition, the lubricant composition includes following components:65-95 weights
Measure lubricating base oil, the composite aluminum base thickening agent of 5-35 weight % and the additive of 0.1-15 weight % of %, the additive
Compound containing structure shown in formula (I):
Preferably, on the basis of the weight of lubricant composition, the lubricant composition includes following components:75-88
The additive of the lubricating base oil of weight %, the composite aluminum base thickening agent of 5-15 weight % and 0.1-5 weight %.
Preferably, on the basis of the weight of lubricant composition, the content of the compound of structure shown in formula (I) is 0.1-3
Weight %, more preferably 0.2-1 weight %.
On the other hand, the present invention provides a kind of preparation sides of the excellent composite aluminum base grease composition of antioxygen property
Method, the described method includes:
(1) lubricating base oil of 1/5-2/5, higher fatty acids, silicon source heat temperature raising are subjected to saponification, then added in
The small molecule acid being dissolved in the lubricating base oil of 1/10-1/5 carries out recombination reaction;
(2) plus water cools down, and then heats to 200-220 DEG C and is refined;
(3) remaining lubricating base oil is added in, 100-130 DEG C is cooled to, then adds in additive;
(4) ground 2-4 times by three-roller;
Wherein, on the basis of the weight of lubricant composition, the dosage of lubricating base oil is 65-95 weight %, by advanced
The dosage of composite aluminum base thickening agent prepared by aliphatic acid, small molecule acid and silicon source is 5-35 weight %, and the dosage of additive is
0.1-15 weight %, which is characterized in that the additive contains the compound of structure shown in formula (I):
Preferably, on the basis of the weight of lubricant composition, the dosage of lubricating base oil is 75-88 weight %, by height
The dosage of composite aluminum base thickening agent prepared by grade aliphatic acid, small molecule acid and silicon source is 5-15 weight %, and the dosage of additive is
0.1-5 weight %.
Preferably, on the basis of the weight of lubricant composition, the dosage of the compound of structure shown in formula (I) is 0.1-3
Weight %, more preferably 0.2-1 weight %.
Lubricant composition provided by the invention has good mechanical stability, water-resistance and colloid stability, more exists
There is apparent advantage on antioxygenic property, and have good compatibility with other lubricating grease.The fat is competent in various
Motor, generator, air blower, transportation, the lubrication of iron and steel enterprise and other various industrial equipments, especially suitable for various
The lubrication of the friction part of mechanical equipment under higher temperature wet condition.
Other features and advantages of the present invention will be described in detail in subsequent specific embodiment part.
Specific embodiment
The specific embodiment of the present invention is described in detail below.It is it should be appreciated that described herein specific
Embodiment is merely to illustrate and explain the present invention, and is not intended to limit the invention.
The present invention provides the composite aluminum base grease composition that a kind of antioxygen property is excellent, with the weight of lubricant composition
On the basis of amount, lubricant composition includes following components:The lubricating base oil of 65-95 weight %, the clad aluminum of 5-35 weight %
The additive of base thickening agent and 0.1-15 weight %, additive contain the compound of structure shown in formula (I):
In the present invention, what antioxidant referred to is the compound of structure shown in formula (I).
In the present invention, it is preferable that on the basis of the weight of lubricant composition, the lubricant composition is included with the following group
Point:The additive of the lubricating base oil of 75-88 weight %, the composite aluminum base thickening agent of 5-15 weight % and 0.1-5 weight %.
In the present invention, on the basis of the weight of lubricant composition, the content of the compound of structure is preferably shown in formula (I)
0.1-3 weight %, more preferably 0.2-1 weight %.
It is contemplated that contain the compound of structure shown in formula (I) by the additive in composite aluminum base grease composition
And realize goal of the invention, even if composite aluminum base grease composition has the excellent performances such as anti-oxidant.Therefore, for clad aluminum
The selection of each conventional constituents, does not limit specifically in base grease.
In the present invention, lubricating base oil can be lubricating base oil commonly used in the art, such as can be mineral oil,
At least one of vegetable oil and synthetic oil.100 DEG C of kinematic viscosity of lubricating base oil are preferably 5-60mm2/ s, more preferably 10-
30mm2/s.For the specific species of mineral oil, vegetable oil and synthetic oil, also there is no particular limitation, and it is normal that this field may be employed
Mineral oil, vegetable oil and synthetic oil, for example, mineral oil can select paraffinic base, cycloalkyl series, vegetable oil can be castor
At least one of sesame oil, rapeseed oil, peanut oil and soybean oil etc., synthetic oil can be poly-a-olefin oil (PAO), Esters oil, fluorine
At least one of oil and silicone oil etc..
In the present invention, composite aluminum base thickening agent can be composite aluminum base thickening agent commonly used in the art, for example, can be acid
It reacts and generates with silicon source, acid includes higher fatty acids and small molecule acid.
Wherein, higher fatty acids can be the aliphatic acid of C12-C25, be preferably lauric acid, palmitic acid, stearic acid and 12-
At least one of hydroxy stearic acid, more preferably stearic acid and/or 12- hydroxy stearic acids.
Wherein, small molecule acid is preferably the carboxylic acid of C4-C11, more preferably benzoic acid, terephthalic acid (TPA), azelaic acid and the last of the ten Heavenly stems
At least one of diacid.
Wherein, silicon source is preferably aluminium isopropoxide and/or aluminium isopropoxide tripolymer.
Above-mentioned composite aluminum base thickening agent may be employed the thinkable various methods of those skilled in the art institute and obtain.
In the present invention, since the antioxidant of structure shown in formula (I) and other additives have preferable compatibility,
According to the use needs of lubricating grease, additive of the invention can also contain antirust agent.For antirust agent species and content without
The species and content of this field routine may be employed in particular/special requirement.For example, antirust agent can be barium mahogany sulfonate, dinonyl benzene
At least one of barium sulfonate and Lanolin Calcium Soap, the content of antirust agent can account for the 0.05-4.5 of lubricant composition total weight
Weight % is preferably 0.1-2 weight %.
In the present invention, the preparation method of the compound of structure preferably includes shown in formula (I):
(a) 2,6- DI-tert-butylphenol compounds, formaldehyde and benzene are subjected to condensation reaction, generate the intermediate M shown in formula (II),
(b) the intermediate M that step (a) obtains with bromide reagent is contacted and carries out bromo-reaction, generated shown in formula (III)
Bromination product,
(c) bromination product that step (b) obtains is made to be contacted with formula (IV) compound represented and carries out coupling reaction, production
(I) antioxidant shown in,
In step (a) of the present invention, the condition of condensation reaction preferably includes:Under an inert atmosphere, in the first solvent,
In the presence of one catalyst, 15- is risen to after 2,6- DI-tert-butylphenol compounds, formaldehyde and benzene are reacted 0.5-1.5h at -20-0 DEG C
30 DEG C, it is then heated to 70-80 DEG C of reaction 1-3h.
In the present invention, inert atmosphere can be the inert atmosphere of this field routine, such as can be by gases such as nitrogen, argon gas
It provides.
It will be understood by those skilled in the art that in order to carry out stable reaction, 0.5-1.5h is reacted at -20-0 DEG C
After rise to 15-30 DEG C, it should be to slowly warm up to 15-30 DEG C, for example, can by -20-0 DEG C react 0.5-1.5h after body
System is placed under 15-30 DEG C of environment temperature, and reaction system itself is made to be to slowly warm up to 15-30 DEG C.
In the present invention, the first solvent is preferably selected from least one in methanol, ethyl alcohol, n,N-Dimethylformamide and acetonitrile
Kind, methanol and/or acetonitrile are more preferably, is still more preferably methanol.
In the present invention, the first catalyst can be inorganic acid or organic acid, be preferably selected from acetic acid, p-methylbenzoic acid and benzene
At least one of sulfonic acid, more preferably acetic acid.
In the present invention, the dosage of 2,6- DI-tert-butylphenol compounds, formaldehyde and benzene is substantially equimolar amounts, but formaldehyde and benzene can
With appropriate excessive.The molar ratio of 2,6 di t butyl phenol, formaldehyde and benzene is preferably 0.9-1.5:0.9-10:0.9-10.
In step (a) of the present invention, the dosage of the first catalyst can be catalytic amount, with mole of 2,6- DI-tert-butylphenol compounds
On the basis of number, the dosage of the first catalyst is preferably 5-100 moles of %, more preferably 10-30 moles of %.
It will be understood by those skilled in the art that in step (a) of the present invention, purer intermediate M, goes back in order to obtain
It needing to post-process the system after reaction, the mode of post processing can include solvent is removed under reduced pressure, then diluted through solvent,
Washing, dry, decompression remove solvent again, for example, the system after reaction is removed into solvent at 0.01-0.05MPa, 40-60 DEG C,
It is subsequently poured into the ethyl acetate (or dichloromethane) of 1-10 times of volume, respectively with distilled water and saturated common salt water washing, then
The drier such as anhydrous calcium chloride or anhydrous sodium sulfate are added at 15-30 DEG C, keep 10-60min.It is filtered to remove drier
Afterwards, solvent is removed at 0.01-0.05MPa, 40-60 DEG C, to obtain intermediate M.
In step (a) of the present invention, 2,6- DI-tert-butylphenol compounds, formaldehyde and benzene carry out the reaction equation of condensation reaction as schemed
Shown in 1, in Fig. 1, the first solvent is using methanol, and the first catalyst is using acetic acid, purpose by way of example only, no
The scope of the present invention is construed as limiting.
In step (b) of the present invention, the condition of bromo-reaction preferably includes:Under an inert atmosphere, in the second solvent,
In the presence of two catalyst, under the conditions of being protected from light, intermediate M that step (a) obtains is reacted with bromide reagent at 15-30 DEG C
Then 1-2h is quenched with quencher.
" inert atmosphere " is as previously mentioned, details are not described herein.
It will be understood by those skilled in the art that more stably being carried out to react, slowly add preferably into intermediate M
Enter brominated reagent.
In the present invention, the second solvent is preferably selected from least one of tetrahydrofuran, dichloromethane, chloroform and ether, more
Preferably tetrahydrofuran.
In the present invention, the second catalyst is preferably selected from ammonium nitrate, benzoyl peroxide (BPO) and azodiisobutyronitrile
At least one of (AIBN).
In the present invention, bromide reagent is preferably N-bromosuccinimide (NBS) and/or Br2, more preferably NBS.
In step (b) of the present invention, it is quenched with quencher, quencher can be quencher commonly used in the art, such as
It can be saturated salt solution.
In step (b) of the present invention, the dosage of intermediate M and bromide reagent is substantially equimolar amounts, but bromide reagent one
As can be suitably excessive, reach 1.1-3 times of equivalent of reaction substrate.Intermediate M and bromide reagent molar ratio are preferably 0.9-
1.2:0.9-3.0。
In step (b) of the present invention, the dosage of the second catalyst can be catalytic amount, on the basis of the molal quantity of intermediate M,
The dosage of second catalyst is preferably 10-100 moles of %, more preferably 40-60 moles of %.
In the method for the present invention step (b), intermediate M contacts the reaction equation for carrying out bromo-reaction with bromide reagent as schemed
Shown in 2, in Fig. 2, bromide reagent is not construed as limiting the scope of the present invention using NBS, purpose by way of example only.
In step (b) of the present invention, in addition to the bromination product shown in generation formula (III), there is the bromo production at micro ortho position
Object generates, and is generated without the bromination product of meta position, but the amount of the bromination product at ortho position very pettiness, to subsequent reactions without substantive shadow
It rings, can be ignored.
It will be understood by those skilled in the art that in step (b) of the present invention, purer bromination product in order to obtain,
It also needs to post-process the system after being quenched, the mode of post processing can include washing, drying, solvent, example is removed under reduced pressure
Such as, the system after being quenched is washed with distilled water, it is dry that anhydrous calcium chloride or anhydrous sodium sulfate etc. is then added at 15-30 DEG C
Drying prescription keeps 10-60min.After being filtered to remove drier, solvent is removed at 0.01-0.05MPa, 40-60 DEG C, to obtain bromine
For product.
In step (c) of the present invention, the condition of coupling reaction preferably includes:Under an inert atmosphere, in the 3rd solvent,
In the presence of three catalyst, the bromination product that step (b) obtains and formula (IV) compound represented are reacted at 80-100 DEG C
4-8h。
" inert atmosphere " is as previously mentioned, details are not described herein.
In the present invention, in order to carry out stable reaction, 80-100 DEG C is preferably gradually heating to, it is then anti-at 80-100 DEG C
Answer 4-8h.
In the present invention, the 3rd solvent is preferably selected from least one of dichloromethane, chloroform, toluene and tetrahydrofuran, more
Preferably dichloromethane.
In the present invention, the 3rd catalyst preferably includes palladium salt, ligand and alkali.Palladium salt is preferably selected from palladium and/or palladium-two
BENZYLIDENE ACETONE complex compound [Pd2(dba)3];Ligand is preferably selected from tri-tert phosphorus, dinaphthol (BINAP) and double (diphenylphosphines
At least one of base) ferrocene (dppf);Alkali is preferably selected from sodium tert-butoxide, potassium tert-butoxide, cesium carbonate and sodium carbonate extremely
Few one kind.
In step (c) of the present invention, bromination product and the dosage of formula (IV) compound represented that step (b) obtains are substantially
For equimolar amounts, but formula (IV) compound represented can be suitably excessive.Shown in the bromination product and formula (IV) that step (b) obtains
The molar ratio of compound be preferably 0.9-1.5:0.9-2.5.
In step (c) of the present invention, the dosage of catalyst can be catalytic amount, on the basis of the molal quantity of bromination product, palladium
The dosage of salt is preferably 5-50 moles of %, more preferably 5-20 moles of %, is still more preferably 5-10 moles of %;The use of ligand
Amount is preferably 5-50 moles of %, more preferably 10-30 moles of %;The dosage of alkali is preferably 5-50 moles of %, more preferably 10-30
Mole %.
In step (c) of the present invention, bromination product that step (b) obtains is contacted with formula (IV) compound represented to be coupled
The reaction equation of reaction is as shown in figure 3, in Fig. 3, and palladium salt is using palladium, purpose by way of example only, not to this
The scope of invention is construed as limiting.
It will be understood by those skilled in the art that purer final product, i.e. antioxygen shown in formula (I) in order to obtain
Agent, the method for the present invention, which preferably further includes, post-processes the system after reaction, and the mode of post processing can include filtering, solvent
Dilution washes, is dry, solvent is removed under reduced pressure, for example, the filtrate after the system filtering after reaction to be poured into the second of 1-10 times of volume
It in acetoacetic ester (or dichloromethane), is then washed with distilled water, anhydrous calcium chloride or anhydrous sulphur is then added at 15-30 DEG C
The drier such as sour sodium keep 10-60min.After being filtered to remove drier, solvent is removed at 0.01-0.05MPa, 40-60 DEG C,
To obtain the antioxidant shown in formula (I).
Each step that the method for the compound of structure shown in formula (I) is prepared in the present invention preferably carries out under stiring, for
Mixing speed can be the mixing speed of this field routine, for example, mixing speed can be 100-800rpm without particular/special requirement.
The present invention is prepared in the method for the compound of structure shown in formula (I), molten for the first solvent, the second solvent and the 3rd
The amount of agent can be the solvent dosage of this field routine, this is known to those skilled in the art, herein no longer without particular/special requirement
It repeats.
As described above, it is contemplated that knot shown in formula (I) is contained by the additive in composite aluminum base grease composition
The compound of structure and realize goal of the invention, even if lubricant composition has the excellent performances such as anti-oxidant.Therefore, for compound
Without particular/special requirement method commonly used in the art may be employed, for example, second aspect, sheet in the preparation method of aluminium-base grease
Invention additionally provides a kind of preparation method of the excellent composite aluminum base grease composition of antioxygen property, and this method includes:
(1) lubricating base oil of 1/5-2/5, higher fatty acids, silicon source heat temperature raising are subjected to saponification, then added in
The small molecule acid being dissolved in the lubricating base oil of 1/10-1/5 carries out recombination reaction;
(2) plus water cools down, and then heats to 200-220 DEG C and is refined;
(3) remaining lubricating base oil is added in, 100-130 DEG C is cooled to, then adds in additive;
(4) ground 2-4 times by three-roller;
Wherein, on the basis of the weight of lubricant composition, the dosage of lubricating base oil is 65-95 weight %, by advanced
The dosage of composite aluminum base thickening agent prepared by aliphatic acid, small molecule acid and silicon source is 5-35 weight %, and the dosage of additive is
0.1-15 weight %, additive contain the compound of structure shown in formula (I):
In the method for the present invention, it is preferable that on the basis of the weight of lubricant composition, the dosage of lubricating base oil is 75-
88 weight %, the dosage of the composite aluminum base thickening agent prepared by higher fatty acids, small molecule acid and silicon source are 5-15 weight %, are added
The dosage for adding agent is 0.1-5 weight %.
In the method for the present invention, the molar ratio of the total amount and silicon source of higher fatty acids and small molecule acid is preferably stoichiometry
Than silicon source can also excess 1-10 weight %.The molar ratio of higher fatty acids and small molecule acid is preferably 1:0.1-5, more preferably
For 1:0.3-2.It will be understood by those skilled in the art that it is answered according to what is prepared by higher fatty acids, small molecule acid and silicon source
The dosage of aluminium base thickening agent is closed, counter can release the dosage of higher fatty acids, small molecule acid and silicon source, this is people in the art
Well known to member, details are not described herein.
In the method for the present invention, on the basis of the weight of lubricant composition, the dosage of the compound of structure is excellent shown in formula (I)
Elect 0.1-3 weight % as, more preferably 0.2-1 weight %.
In the method for the present invention, the lubricating base oil of 1/5-2/5, the lubricating base oil of 1/10-1/5 refer respectively to account for lubrication base
1/5-2/5,1/10-1/5 of plinth oil total amount.
In the method for the present invention step (1), 90-120 DEG C is preferably heated to, the saponification time is preferably 0.5-
1.5h, complex reaction time are preferably 0.5-1.5h.
In the method for the present invention step (2), add the amount of water temperature is preferably made to be down to 70-90 DEG C, and preferably keep the temperature 5-25min.
In the method for the present invention step (2), the time of refining is preferably 5-25min.
Each step of the method for the present invention preferably carries out under stiring, can be this field for mixing speed without particular/special requirement
Conventional mixing speed, for example, mixing speed can be 20-500rpm.
Lubricating base oil, higher fatty acids, small molecule acid, silicon source, additive are as previously mentioned, details are not described herein.