Detailed description of the invention
Below the specific embodiment of the present invention is elaborated. Should be understood that, retouch in this placeThe detailed description of the invention of stating only, for description and interpretation the present invention, is not limited to the present invention.
The invention provides a kind of composite aluminum base grease composition of antioxygen property excellence, with lubricating grease groupThe weight of compound is benchmark, and lubricant composition comprises following component: the lubrication base of 65-95 % by weightOil, the composite aluminum base thickening agent of 5-35 % by weight and the additive of 0.1-15 % by weight, additive contains formula(I) compound of structure shown in:
In the present invention, what antioxidant referred to is the compound of structure shown in formula (I).
In the present invention, preferably, taking the weight of lubricant composition as benchmark, described lubricant compositionComprise following component: the lubricating base oil of 75-88 % by weight, the composite aluminum base thickening agent of 5-15 % by weightAdditive with 0.1-5 % by weight.
In the present invention, taking the weight of lubricant composition as benchmark, the compound of structure shown in formula (I)Content be preferably 0.1-3 % by weight, more preferably 0.2-1 % by weight.
The present invention is intended to contain knot shown in formula (I) by the additive in composite aluminum base grease compositionThe compound of structure and realize goal of the invention, good anti-oxidant even if composite aluminum base grease composition hasEtc. performance. Therefore, for the selection of each conventional component in composite aluminum base grease, all less than specific limitSystem.
In the present invention, lubricating base oil can be the conventional lubricating base oil using in this area, for example canFor at least one in mineral oil, vegetable oil and artificial oil. 100 DEG C of kinematic viscosity of lubricating base oil are preferredFor 5-60mm2/ s, more preferably 10-30mm2/ s. Concrete for mineral oil, vegetable oil and artificial oilAlso there is no particular limitation for kind, can adopt the conventional mineral oil in this area, vegetable oil and artificial oil,For example, mineral oil can be selected paraffinic base, cycloalkyl series, vegetable oil can be castor oil, rapeseed oil,At least one in peanut oil and soybean wet goods, artificial oil can be poly-a-olefin oil (PAO), ester class oil,At least one in fluorocarbon oil and silicone oil etc.
In the present invention, composite aluminum base thickening agent can be the conventional composite aluminum base thickening agent in this area, for example,Can be that acid is reacted generation with aluminium source, acid comprises higher fatty acids and little molecule acid.
Wherein, higher fatty acids can be the aliphatic acid of C12-C25, be preferably laurate, palmitic acid,At least one in stearic acid and 12-hydroxy stearic acid, more preferably stearic acid and/or 12-hydroxyl tristearinAcid.
Wherein, little molecule acid is preferably the carboxylic acid of C4-C11, more preferably benzoic acid, terephthalic acid (TPA),At least one in azelaic acid and decanedioic acid.
Wherein, aluminium source is preferably aluminium isopropoxide and/or aluminium isopropoxide tripolymer.
Above-mentioned composite aluminum base thickening agent can adopt the thinkable the whole bag of tricks of those skilled in the art to obtain.
In the present invention, because having preferably, the antioxidant of structure shown in formula (I) and other additives joinWu Xing, therefore, according to the use needs of lubricating grease, additive of the present invention can also contain antirust agent.Without particular/special requirement, can adopt kind and the content of this area routine for the kind of antirust agent and content.For example, antirust agent can be at least one in barium mahogany sulfonate, dinonyl barium benzosulfonate and Lanolin Calcium SoapKind, the content of antirust agent can account for the 0.05-4.5 % by weight of lubricant composition gross weight, is preferably 0.1-2% by weight.
In the present invention, shown in formula (I), the preparation method of the compound of structure preferably includes:
(a) 2,6-DI-tert-butylphenol compounds, formaldehyde and benzene are carried out to condensation reaction, shown in production (II)Intermediate M,
(b) intermediate M step (a) being obtained contacts with bromide reagent and carries out bromo-reaction, rawBromination product shown in an accepted way of doing sth (III),
(c) make the bromination product that step (b) obtains contact and carry out idol with the compound shown in formula (IV)Connection reaction, the antioxidant shown in production (I),
In step of the present invention (a), the condition of condensation reaction preferably includes: under inert atmosphere,In one solvent, under the existence of the first catalyst, by 2,6-DI-tert-butylphenol compounds, formaldehyde and benzene at-20-0 DEG CAfter lower reaction 0.5-1.5h, rise to 15-30 DEG C, be then heated to 70-80 DEG C of reaction 1-3h.
In the present invention, inert atmosphere can be the inert atmosphere of this area routine, for example can by nitrogen,The gases such as argon gas provide.
It will be understood by those skilled in the art that for stable reaction is carried out reaction at-20-0 DEG CAfter 0.5-1.5h, rise to 15-30 DEG C, should slowly be warming up to 15-30 DEG C, for example, can be by-20-0 DEG CSystem after lower reaction 0.5-1.5h is placed under the environment temperature of 15-30 DEG C, makes reaction system self slowBe warming up to 15-30 DEG C.
In the present invention, the first solvent is preferably selected from methyl alcohol, ethanol, DMF and acetonitrileAt least one, more preferably methyl alcohol and/or acetonitrile, is further preferably methyl alcohol.
In the present invention, the first catalyst can be inorganic acid or organic acid, is preferably selected from acetic acid, to methylAt least one in benzoic acid and benzene sulfonic acid, more preferably acetic acid.
In the present invention, the consumption of 2,6-DI-tert-butylphenol compounds, formaldehyde and benzene is essentially equimolar amounts, butFormaldehyde and benzene can be suitably excessive. The mol ratio of 2,6-DI-tert-butylphenol compounds, formaldehyde and benzene is preferably0.9-1.5:0.9-10:0.9-10。
In step of the present invention (a), the consumption of the first catalyst can be catalytic amount, with the tertiary fourth of 2,6-bis-The molal quantity of base phenol is benchmark, and the consumption of the first catalyst is preferably 5-100 % by mole, more preferably10-30 % by mole.
It will be understood by those skilled in the art that in step of the present invention (a), purer in order to obtainIntermediate M, also need reacted system to carry out post processing, the mode of post processing can comprise and subtractingPress except desolventizing, then through solvent dilution, washing, dry, decompression again except desolventizing, for example, will be anti-Should after system at 0.01-0.05MPa, 40-60 DEG C except desolventizing, then pour 1-10 times of volume intoIn ethyl acetate (or carrene), use respectively distilled water and saturated common salt water washing, then at 15-30 DEG CUnder add the drier such as anhydrous calcium chloride or anhydrous sodium sulfate, keep 10-60min. Remove by filter dryAfter agent, at 0.01-0.05MPa, 40-60 DEG C, remove desolventizing, to obtain intermediate M.
In step of the present invention (a), 2,6-DI-tert-butylphenol compounds, formaldehyde and benzene carry out the reaction of condensation reactionAs shown in Figure 1, in Fig. 1, what the first solvent adopted is methyl alcohol to equation, and what the first catalyst adopted isAcetic acid, only for purposes of illustration, is not construed as limiting scope of the present invention.
In step of the present invention (b), the condition of bromo-reaction preferably includes: under inert atmosphere,In two solvents, under the existence of the second catalyst, under lucifuge condition, during step (a) is obtainedMesosome M reacts 1-2h with bromide reagent at 15-30 DEG C, then uses quencher cancellation.
" inert atmosphere " as previously mentioned, do not repeat them here.
To it will be understood by those skilled in the art that in order reacting more stably and to carry out, preferably to intermediateIn M, slowly add brominated reagent.
In the present invention, the second solvent is preferably selected from oxolane, carrene, chloroform and ether extremelyFew a kind of, more preferably oxolane.
In the present invention, the second catalyst is preferably selected from ammonium nitrate, benzoyl peroxide (BPO) and azoAt least one in bis-isobutyronitrile (AIBN).
In the present invention, bromide reagent is preferably N-bromosuccinimide (NBS) and/or Br2, more excellentElect NBS as.
In step of the present invention (b), carry out cancellation with quencher, quencher can be conventional for this areaQuencher can be for example saturated aqueous common salt.
In step of the present invention (b), the consumption of intermediate M and bromide reagent is essentially equimolar amounts,But bromide reagent generally can be suitably excessive, reach 1.1-3 times of equivalent of reaction substrate. Intermediate M withBromide reagent mol ratio is preferably 0.9-1.2:0.9-3.0.
In step of the present invention (b), the consumption of the second catalyst can be catalytic amount, with intermediate M'sMolal quantity is benchmark, and the consumption of the second catalyst is preferably 10-100 % by mole, and more preferably 40-60 rubsYou are %.
In the inventive method step (b), intermediate M contacts with bromide reagent and carries out the anti-of bromo-reactionAnswer equation as shown in Figure 2, in Fig. 2, that bromide reagent adopts is NBS, is only illustrational order, scope of the present invention is not construed as limiting.
In step of the present invention (b), except the bromination product shown in production (III), also has traceThe bromination product at ortho position generates, and between not having, the bromination product of position generates, but the amount of the bromination product at ortho position veryPettiness, does not have materially affect to subsequent reactions, negligible.
It will be understood by those skilled in the art that in step of the present invention (b), purer in order to obtainBromination product, also need the system after cancellation to carry out post processing, the mode of post processing can comprise waterWash, be dried, removal of solvent under reduced pressure, for example, the system after cancellation is washed with distilled water, then existAt 15-30 DEG C, add the drier such as anhydrous calcium chloride or anhydrous sodium sulfate, keep 10-60min. FilterRemove after drier, at 0.01-0.05MPa, 40-60 DEG C, remove desolventizing, to obtain bromination product.
In step of the present invention (c), the condition of coupling reaction preferably includes: under inert atmosphere,In three solvents, under the existence of the 3rd catalyst, the bromination product that step (b) is obtained and formula (IV)Shown compound reacts 4-8h at 80-100 DEG C.
" inert atmosphere " as previously mentioned, do not repeat them here.
In the present invention, for stable reaction is carried out, be preferably warming up to gradually 80-100 DEG C, then existAt 80-100 DEG C, react 4-8h.
In the present invention, the 3rd solvent is preferably selected from carrene, chloroform, toluene and oxolane extremelyFew a kind of, more preferably carrene.
In the present invention, the 3rd catalyst preferably includes palladium salt, part and alkali. Palladium salt is preferably selected from palladiumAnd/or palladium-dibenzalacetone complex compound [Pd2(dba)3]; Part is preferably selected from tri-tert phosphorus, dinaphthol(BINAP) at least one and in two (diphenylphosphino) ferrocene (dppf); Alkali is preferably selected from uncleAt least one in sodium butoxide, potassium tert-butoxide, cesium carbonate and sodium carbonate.
In step of the present invention (c), the chemical combination shown in the bromination product that step (b) obtains and formula (IV)The consumption of thing is essentially equimolar amounts, but the compound shown in formula (IV) can be suitably excessive. Step(b) mol ratio of the compound shown in the bromination product obtaining and formula (IV) is preferably 0.9-1.5:0.9-2.5.
In step of the present invention (c), the consumption of catalyst can be catalytic amount, with bromination product moleNumber is benchmark, and the consumption of palladium salt is preferably 5-50 % by mole, and more preferably 5-20 % by mole more enters oneStep is preferably 5-10 % by mole; The consumption of part is preferably 5-50 % by mole, more preferably 10-30 % by mole;The consumption of alkali is preferably 5-50 % by mole, more preferably 10-30 % by mole.
In step of the present invention (c), the chemical combination shown in the bromination product that step (b) obtains and formula (IV)As shown in Figure 3, in Fig. 3, what palladium salt adopted is acetic acid to the reaction equation that coupling reaction is carried out in thing contactPalladium, only for purposes of illustration, is not construed as limiting scope of the present invention.
It will be understood by those skilled in the art that in order to obtain purer end product i.e. formula (I)Shown antioxidant, the inventive method preferably also comprises reacted system is carried out to post processing, post processingMode can comprise filtration, solvent dilution, washing, dry, removal of solvent under reduced pressure, for example, will be anti-Should after system filter after filtrate pour in the ethyl acetate (or carrene) of 1-10 times of volume,Then with distilled water washing, then at 15-30 DEG C, add anhydrous calcium chloride or anhydrous sodium sulfate etc. dryDrying prescription, keeps 10-60min. Remove by filter after drier, at 0.01-0.05MPa, 40-60 DEG C, removeDesolventizing, to obtain the antioxidant shown in formula (I).
Each step of the method for the compound of structure shown in preparation formula in the present invention (I) preferably under agitationCarrying out, without particular/special requirement, can be the mixing speed of this area routine for mixing speed, for example, stirsThe speed of mixing can be 100-800rpm.
Shown in preparation formula of the present invention (I) in the method for the compound of structure, for the first solvent, secondThe amount of solvent and the 3rd solvent, without particular/special requirement, can be the solvent load of this area routine, and this is abilityField technique personnel are known, do not repeat them here.
As mentioned above, the present invention is intended to contain formula by the additive in composite aluminum base grease composition(I) compound of structure shown in and realize goal of the invention, good anti-even if lubricant composition hasThe performances such as oxidation. Therefore,, can adopt without particular/special requirement for the preparation method of composite aluminum base greaseThe conventional method using in this area, for example, second aspect, the present invention also provides a kind of antioxygen property excellentThe preparation method of different composite aluminum base grease composition, the method comprises:
(1) by the lubricating base oil of 1/5-2/5, higher fatty acids, that aluminium source heat temperature raising carries out saponification is anti-Should, then add the little molecule acid in the lubricating base oil that is dissolved in 1/10-1/5 to carry out recombination reaction;
(2) add water and lower the temperature, be then warming up to 200-220 DEG C and refine;
(3) add residue lubricating base oil, be cooled to 100-130 DEG C, then add additive;
(4) grind 2-4 time by three-roller;
Wherein, taking the weight of lubricant composition as benchmark, the consumption of lubricating base oil is that 65-95 is heavyThe consumption of the composite aluminum base thickening agent of measure %, being prepared by higher fatty acids, little molecule acid and aluminium source is 5-35% by weight, the consumption of additive is 0.1-15 % by weight, the chemical combination that additive contains structure shown in formula (I)Thing:
In the inventive method, preferably, taking the weight of lubricant composition as benchmark, lubricating base oilThe composite aluminum base multiviscosisty that consumption is 75-88 % by weight, prepared by higher fatty acids, little molecule acid and aluminium sourceThe consumption of agent is 5-15 % by weight, and the consumption of additive is 0.1-5 % by weight.
In the inventive method, the total amount of higher fatty acids and little molecule acid and being preferably of mol ratio in aluminium sourceLearn metering ratio, aluminium source also can excessive 1-10 % by weight. The mol ratio of higher fatty acids and little molecule acid is excellentElect 1:0.1-5 as, more preferably 1:0.3-2. It will be understood by those skilled in the art that basis is by seniorThe consumption of composite aluminum base thickening agent prepared by aliphatic acid, little molecule acid and aluminium source, can instead release senior fatThe consumption in fat acid, little molecule acid and aluminium source, this is conventionally known to one of skill in the art, does not repeat them here.
In the inventive method, taking the weight of lubricant composition as benchmark, the change of structure shown in formula (I)The consumption of compound is preferably 0.1-3 % by weight, more preferably 0.2-1 % by weight.
In the inventive method, the lubricating base oil of 1/5-2/5, the lubricating base oil of 1/10-1/5 refer to respectivelyAccount for 1/5-2/5, the 1/10-1/5 of lubricating base oil total amount.
In the inventive method step (1), be preferably heated to 90-120 DEG C, the saponification time is excellentElect 0.5-1.5h as, complex reaction time is preferably 0.5-1.5h.
In the inventive method step (2), the amount adding water preferably makes temperature be down to 70-90 DEG C, and preferably protectsTemperature 5-25min.
In the inventive method step (2), the time of refining is preferably 5-25min.
The each step of the inventive method is preferably under agitation carried out, for mixing speed without particular/special requirement, canFor the mixing speed of this area routine, for example, mixing speed can be 20-500rpm.
Lubricating base oil, higher fatty acids, little molecule acid, aluminium source, additive as previously mentioned, at this notRepeat again.