Embodiment
The embodiment to the present invention is described in detail below.It should be appreciated that this place is retouched
The embodiment stated is merely to illustrate and explain the present invention, and is not intended to limit the invention.
On the one hand, the invention provides a kind of high-temperature chain oil composition, with the weight of lubricant oil composite
On the basis of, lubricant oil composite contains following components:85-99 weight % lube base oil, 0.01-10
The weight % wear-resistant multipurpose additive of antioxygen, 0.01-5 weight % thiophenols ester type antioxidant, 0.05-5
Weight % Zinc oxide nanoparticle, 0.01-5 weight % demulsifier, the wear-resistant multipurpose additive of antioxygen is
The compound of structure shown in formula (I):
In the present invention, on the basis of the weight of lubricant oil composite, the content of lube base oil is preferably
90-99 weight %;The content of the wear-resistant multipurpose additive of antioxygen is preferably 0.02-5 weight %, more preferably
0.1-4 weight %;The content of thiophenols ester type antioxidant is preferably 0.05-3 weight %;Zinc-oxide nano
The content of grain is preferably 0.1-4 weight %, more preferably 0.1-3 weight %;The content of demulsifier is preferably
0.02-4 weight %, more preferably 0.05-3 weight %.
It is contemplated that the compound by containing structure shown in formula (I) in lubricant oil composite, and
The compound of structure shown in formula (I) is combined with thiophenols ester type antioxidant and realizes goal of the invention, even if
Lubricant oil composite has the excellent performance such as wear-resistant and anti-oxidant.Therefore, in lubricant oil composite
The selection of each conventional constituents, is not limited specifically.
In the present invention, lube base oil can be lube base oil commonly used in the art, for example
Can be mineral lubricating oil and/or synthetic lubricant fluid.
Mineral lubricating oil can be from light fraction mineral oil to heavy distillat mineral oil in viscosity, including liquid stone
Wax oil and hydrofinishing, the alkane that solvent is treated, cycloalkanes and mixing par-affinic-naphthenic types mineral lubricant
Oil, is generally divided into I, II, Group III base oil, and common trade names include I classes 150SN, 600SN,
II classes 100N, 150N, 350N etc..
Synthetic lubricant fluid can include polymerization hydrocarbon ils, alkyl benzene and its derivative, polymerize the specific example of hydrocarbon ils
Son includes but is not limited to polybutene, polypropylene, propylene-isobutylene copolymers, the polybutene of chlorination, poly- (1-
Hexene), poly- (1- octenes), poly- (1- decene), common trade names include PAO4, PAO6, PAO8,
PAO10 etc., alkyl benzene and its derivative specific example includes but is not limited to detergent alkylate, the tetradecane
Base benzene, dinonyl benzene, two (2- ethylhexyls) benzene, alkyl benzene derivate include the diphenyl ether of alkylation
Diphenyl sulfide and its derivative, analog and homologue with alkylation etc..
Another suitable type of synthetic lubricant fluid can be Esters oil, including dicarboxylic acids (such as phthalic acid,
It is butanedioic acid, alkyl succinic acid and alkenyl succinic acid, maleic acid, azelaic acid, suberic acid, decanedioic acid, anti-
Butene dioic acid, adipic acid, linoleic acid dimer, malonic acid, alkyl malonic acid, alkenyl malonic) with
Various alcohol (such as butanol, hexanol, dodecyl alcohol, 2- ethylhexyl alcohols, ethylene glycol, propane diols) hairs
The ester or complex ester of raw condensation reaction generation.The specific example of these esters includes but is not limited to the fourth of adipic acid two
Ester, decanedioic acid two (2- ethylhexyls) ester, the just own ester of fumaric acid acid two, di-n-octyl sebacate, nonyl
Diacid di-isooctyl, two different decayl esters of azelaic acid, dioctyl phthalate, didecyl phthalate,
Decanedioic acid two (larane base) ester, 2- ethylhexyl diester of linoleic acid dimer etc..
Another suitable type of synthetic lubricant fluid can be for fischer tropsch process synthetic hydrocarbon oil and to this synthesis hydrocarbon
Oil by hydroisomerizing, be hydrocracked, the lube base oil that the PROCESS FOR TREATMENT such as dewax is obtained.
In the present invention, lube base oil preferred viscosities index is more than 80, saturated hydrocarbon content and is more than 90 weights
Measure the lube base oil that %, sulfur content are less than 0.03 weight %.
In the present invention, thiophenols ester type antioxidant can be thiophenols ester type antioxidant commonly used in the art,
For example can for the double lauryl alcohol esters (DLTDP) of thio-2 acid, the double octadecyl esters (DSTDP) of thio-2 acid,
2,5- dimercapto -1,3,4- thiadiazoles (DMTD) and 2,2'- thiobis [3- (3,5- di-t-butyl -4- hydroxy benzenes
At least one of base) ethyl propionate], preferably 2,2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl)
Ethyl propionate], such as antioxidant 1035 of Sichuan Yong Ye Chemical Co., Ltd.s production, German BASF is public
Take charge of the IRGANOX L115 of production.
In the present invention, Zinc oxide nanoparticle is the single or composite Nano of the composition containing Zinc oxide nanoparticle
Particle.The high-temperature chain lubricating oil of addition Zinc oxide nanoparticle has preferable high temperature wear resistance, adds
Plus the abrasion resistance of rear oil product is improved.The particle diameter of nano-particle is 3-150nm.
In the present invention, demulsifier can be propylene glycol block polyether, NPE, ethylenediamine
At least one of polyoxypropylene polyoxyethylene ether and propane diamine polyoxypropylene polyoxyethylene ether.
The lubricant oil composite of the present invention can also contain at least one of antirust agent and anti-foaming agent.Antirust
Agent can be selected from imidazoles and/or alkenyl succinic acid esters, preferably 4,5- glyoxalidine, alkenyl imidazoline
At least one of succinate and alkenyl succinic acid ester, for example can be from the safe lubricating oil addition in Jinzhou
T746, T703, T747 of agent Co., Ltd production.Anti-foaming agent can select polysiloxane type anti-foaming agent,
For example can be silicone oil and/or dimethyl silicone polymer.For the content of antirust agent, pour-point depressant and anti-foaming agent
Can be the conventional content in this area, this is known to those skilled in the art, herein without particular/special requirement
Repeat no more.
In the present invention, the preparation method of the compound of structure is preferably included shown in formula (I):
(a) aniline, sulfur chloride and 4- chloroanilines are reacted, the intermediate shown in generation formula (II)
M,
(b) the intermediate M for obtaining step (a) and dimercapto -1,3,4- thiadiazoles be in the basic conditions
Nucleophilic substitution is carried out, the multipurpose additive shown in formula (I) is generated,
In step (a) of the present invention, the concrete mode that aniline, sulfur chloride and 4- chloroanilines are reacted
Preferably include:
(i) under an inert atmosphere, in the first solvent, by aniline and sulfur chloride at -20-0 DEG C fully
Reacted;
(ii) 4- chloroanilines are added in the reaction system of step (i), 1-3h is reacted at 15-30 DEG C.
In the present invention, inert atmosphere can be the conventional inert atmosphere in this area, for example can by nitrogen,
The gases such as argon gas are provided.
In step (i) of the present invention, the first solvent be preferably selected from dichloromethane, tetrahydrofuran, toluene,
At least one of dimethylbenzene and dioxane, more preferably dichloromethane and/or tetrahydrofuran, more enter one
Step is preferably dichloromethane.
In the present invention in step (i), fully reacted and refer to that reaction is complete, i.e., reaction raw materials are complete
Reacted entirely.Reaction can be monitored using method commonly used in the art, to confirm that reaction is complete,
The method such as can use TLC (TLC) or gas-chromatography is monitored.
In step (ii) of the present invention, 1-3h is reacted at 15-30 DEG C, it is preferably fully anti-in step (i)
Ying Hou, 15-30 DEG C is gradually increased to by the temperature of reaction system, is added 4- chloroanilines and is carried out reaction 1-3h.
Under the preferable case, reaction yield can be further improved.
In step (ii) of the present invention, the feed postitions of 4- chloroanilines is preferably to add by several times, for example can be with
Divide 3-4 addition.Under the preferable case, reaction yield can be further improved.Added for gradation
When, each addition can be with identical, can also be different, for easy to operate, preferably each addition
Amount is identical.
In step (ii) of the present invention, 1-3h is reacted, the mode for stopping reaction can be people in the art
The thinkable various modes of member institute, are quenched, quencher can be this for example, quencher can be added
The conventional quencher in field, for example, can be saturated aqueous common salt.
In the present invention, the consumption of aniline, sulfur chloride and 4- chloroanilines is substantially equimolar amounts, but aniline
Can be suitably excessive with sulfur chloride.The mol ratio of aniline, sulfur chloride and 4- chloroanilines is preferably 0.9-1.5:
0.9-1.5:0.8-1.2.
It will be understood by those skilled in the art that in step (a) of the present invention, it is purer in order to obtain
Intermediate M, in addition it is also necessary to reacted system is post-processed, the mode of post processing can include washing
Wash, dry, removal of solvent under reduced pressure, for example, by the reaction system after being quenched respectively use distilled water and saturation
Brine It, then adds the drier such as anhydrous calcium chloride or anhydrous sodium sulfate at 15-30 DEG C,
Keep 10-60min.It is filtered to remove after drier, solvent is removed at 0.01-0.05MPa, 40-60 DEG C,
To obtain intermediate M.
In step (a) of the present invention, the reaction equation that aniline, sulfur chloride and 4- chloroanilines are reacted
As shown in figure 1, in Fig. 1, the first solvent uses dichloromethane, purpose by way of example only,
The scope of the present invention is not construed as limiting.
In step (b) of the present invention, the condition of nucleophilic substitution is preferably included:Under an inert atmosphere,
In the second solvent, dimercapto-1,3,4-thiadiazole, alkaline reagent and catalyst are mixed at 15-30 DEG C
10-30min, then adds intermediate M, is fully reacted.I.e. alkalescence condition is provided by alkaline reagent.
" inert atmosphere ", " fully being reacted " are as it was previously stated, will not be repeated here.
In the present invention, intermediate M is preferably slowly added to, for example, can add by several times, can typically be divided
3-4 addition.Under the preferable case, reaction yield can be further improved.When being added for gradation,
Each addition can be with identical, can also be different, for easy to operate, preferably each addition phase
Together.
In the present invention, the second solvent is preferably selected from dichloromethane, tetrahydrofuran, toluene, dimethylbenzene, N, N-
At least one of dimethylformamide, more preferably dichloromethane and/or DMF,
Still more preferably it is N,N-dimethylformamide.
In the present invention, alkaline reagent is preferably selected from the inorganic bases such as potassium carbonate, sodium carbonate, sodium methoxide extremely
Few one kind.
In the present invention, catalyst is preferably potassium sulfate.
In step (b) of the present invention, the use of dimercapto-1,3,4-thiadiazole, alkaline reagent and intermediate M
Amount is substantially equimolar amounts, but dimercapto-1,3,4-thiadiazole and alkaline reagent can be suitably excessive.Two
The mol ratio of sulfydryl -1,3,4- thiadiazoles, alkaline reagent and intermediate M is preferably 0.9-3.0:0.9-5.0:
0.8-1.5。
In step (b) of the present invention, the consumption of catalyst can be catalytic amount, with dimercapto -1,3,4- thiophenes two
On the basis of the molal quantity of azoles, the consumption of catalyst is preferably 5-100 moles of %, and more preferably 10-50 rubs
You are %.
In step (b) of the present invention, the reaction that dimercapto-1,3,4-thiadiazole and intermediate M are reacted
Equation is as shown in Fig. 2 in Fig. 2, alkaline reagent uses potassium carbonate, mesh by way of example only
, the scope of the present invention is not construed as limiting.
It will be understood by those skilled in the art that in order to obtain purer final product, i.e., it is of the invention
Multipurpose additive, the present invention, which prepares the method for multipurpose additive, preferably also to be included entering reacted system
Row post processing, the mode of post processing can include washing, dry, removal of solvent under reduced pressure, for example, will fill
Reacted system is divided to pour into the ethyl acetate (or dichloromethane) of 1-10 times of volume, respectively with steaming
Distilled water and saturated common salt water washing, then add anhydrous calcium chloride or anhydrous sodium sulfate at 15-30 DEG C
Deng drier, 10-60min is kept.It is filtered to remove after drier, in 0.01-0.05MPa, 40-60 DEG C
Lower removing solvent, to obtain final product.
Each step of the method for the compound of structure shown in formula (I) is prepared in the present invention preferably under agitation
Carry out, can be the conventional mixing speed in this area, for example, stirring for mixing speed without particular/special requirement
It can be 100-800rpm to mix speed.
In the present invention, for the first solvent and the second solvent amount without particular/special requirement, can for this area it is normal
The solvent load of rule, this is known to those skilled in the art, will not be repeated here.
As described above, it is contemplated that passing through the change containing structure shown in formula (I) in lubricant oil composite
Compound, and the compound of structure shown in formula (I) and thiophenols ester type antioxidant is combined and realizes and invent
Purpose, even if lubricant oil composite has the excellent performance such as wear-resistant and anti-oxidant.Therefore, for lubrication
The preparation method of fluid composition can use method commonly used in the art without particular/special requirement, for example,
Second aspect, present invention also offers a kind of preparation method of high-temperature chain oil composition, this method includes:
Lube base oil, the wear-resistant multipurpose additive of antioxygen, thiophenols ester type antioxidant, optional oxygen will be contained
Change zinc nanoparticles, the raw material of optional demulsifier is well mixed and obtains lubricant oil composite, wherein, with
On the basis of the weight of lubricant oil composite, the consumption of lube base oil is 85-99 weight %, antioxygen resists
The consumption of mill multipurpose additive is that 0.01-10 weight %, the consumption of thiophenols ester type antioxidant are 0.01-5
Weight %, the consumption of Zinc oxide nanoparticle are 0.05-5 weight %, and the consumption of demulsifier is 0.01-5 weights
% is measured, the wear-resistant multipurpose additive of antioxygen is the compound of structure shown in formula (I):
In the inventive method, on the basis of the weight of lubricant oil composite, the consumption of lube base oil is excellent
It is preferably 0.02-5 weight % to elect 90-99 weight %, the consumption of the wear-resistant multipurpose additive of antioxygen as, more excellent
It is preferably 0.05-3 weight %, zinc oxide to elect 0.1-4 weight %, the consumption of thiophenols ester type antioxidant as
The consumption of nano particle is preferably 0.1-4 weight %, more preferably 0.1-3 weight %, the consumption of demulsifier
Preferably 0.05-4 weight %, more preferably 0.05-3 weight %.
As it was previously stated, in the inventive method, raw material can also contain in antirust agent, pour-point depressant and anti-foaming agent
At least one.
In the inventive method, for mixing mode without particular/special requirement, can will for example remove lube base
Each raw material components of oil are added separately in lube base oil, can also will be each except lube base oil
Component is mixed and made into concentrate and is then added in lube base oil.
In the inventive method, the condition of mixing is preferably included:Temperature is 40-90 DEG C, and the time is 1-6h.
The wear-resistant multipurpose additive of lube base oil, antioxygen, thiophenols ester type antioxidant, zinc-oxide nano
Particle, demulsifier, antirust agent and anti-foaming agent are as it was previously stated, will not be repeated here.
Embodiment 3
The present embodiment is used to illustrate lubricant oil composite of the present invention and preparation method thereof.
By the S1 of 1.9 parts by weight, the 2,2'- thiobis [3- (3,5- di-t-butyl -4- hydroxy benzenes of 0.1 parts by weight
Base) ethyl propionate], (Turner rice limited material in Shandong is public for the single Zinc oxide nanoparticle of 0.25 parts by weight
Department), the ethylenediamine polyoxypropylene polyoxyethylene ether of 0.5 parts by weight, the poly dimethyl silicon of 0.01 parts by weight
Oxygen alkane (being purchased from Hubei xinsihai Chemical Co., Ltd.) is added to the adipic acid two of 97.39 parts by weight
In butyl ester, 1h is stirred at 90 DEG C, it is well mixed to obtain lubricant oil composite A3.
Comparative example 1
Method according to embodiment 2 prepares lubricant oil composite, unlike, by S1 replace with wait weigh
2, the 2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionate] of part is measured, lubricating oil composition is obtained
Thing D1.
Comparative example 2
Method according to embodiment 2 prepares lubricant oil composite, unlike, by 2,2'- thiobis [3- (3,5-
Di-tert-butyl-hydroxy phenyl) ethyl propionate] S1 of parts by weight such as replace with, obtain lubricant oil composite
D2。
Comparative example 3
Method according to embodiment 2 prepares lubricant oil composite, unlike, by S1 and 2,2'- is thio
Double [3- (3,5- di-tert-butyl-hydroxy phenyls) ethyl propionates] dibutyl dithio of parts by weight such as replace with
Carbaminate, obtains lubricant oil composite D3.
Comparative example 4
Method according to embodiment 2 prepares lubricant oil composite, unlike, by S1 and 2,2'- is thio
Double [3- (3,5- di-tert-butyl-hydroxy phenyls) ethyl propionates] the trimethylphenyl phosphorous of parts by weight such as replace with
Sour zinc, obtains lubricant oil composite D4.
Comparative example 5
Method according to embodiment 2 prepares lubricant oil composite, unlike, by S1 and 2,2'- is thio
Double [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionates] the fourth octyl diphenylamine of parts by weight such as replace with,
Obtain lubricant oil composite D5.
Test case
Lubricant oil composite A1-A3, D1-D5 are tested as follows respectively:
The measure of initial oxidation temperature is carried out using TA5000-DSC2910 differential thermal analyzers;
The measure of oxidation induction period is carried out using high pressure differential scanning amount method (PDSC);
Using tetra-ball machine test method, PB, PD value are determined by GB/T3142;
Wear scar diameter is determined using SH/T 0189.
The sediment yield that oil product when determining 250 DEG C is produced is tested using swash plate coking analog meter.
It the results are shown in Table 1.
Table 1
|
A1 |
A2 |
A3 |
D1 |
D2 |
D3 |
D4 |
D5 |
Initial oxidation temperature, DEG C |
204 |
211 |
219 |
192 |
190 |
198 |
191 |
192 |
Oxidation induction period, min |
43.7 |
50.7 |
58.2 |
32.6 |
37.8 |
33.1 |
29.4 |
31.5 |
PB, kgf |
90 |
100 |
105 |
50 |
65 |
55 |
65 |
50 |
PD, kgf |
295 |
305 |
310 |
225 |
265 |
220 |
240 |
230 |
Wear scar diameter d60 40, mm |
0.53 |
0.47 |
0.46 |
0.69 |
0.61 |
0.71 |
0.62 |
0.64 |
High temperature deposition object amount, mg |
6.9 |
5.5 |
5.1 |
10.2 |
9.6 |
9.2 |
10.3 |
9.7 |
It will be understood by those skilled in the art that initial oxidation temperature is higher, the heat endurance of lubricating oil
Better;Oxidation induction period is longer, and the antioxygenic property of lubricating oil is better;PB, PD value are bigger, lubrication
The wear resistance of oil is better;Wear scar diameter is smaller, and the wear resistance of lubricating oil is better;Coking amount is got over
Height, the high temperature resistance cokeability for representing this test specimen is poorer.
A2 is compared with D1-D5 respectively as can be seen that the lubricant oil composite of the present invention has more
Good inoxidizability and abrasion resistance.
The high-temperature chain oil composition of the present invention has excellent abrasion resistance and antioxygenic property, Ke Yiguang
It is general to be applied to high-temperature chain lubricating area.
The preferred embodiment of the present invention is described in detail above in association with accompanying drawing, still, the present invention is not limited
Detail in above-mentioned embodiment, can be to the present invention in the range of the technology design of the present invention
Technical scheme carry out a variety of simple variants, these simple variants belong to protection scope of the present invention.
It is further to note that each particular technique feature described in above-mentioned embodiment,
In the case of reconcilable, it can be combined by any suitable means, in order to avoid unnecessary
Repeat, the present invention no longer separately illustrates to various possible combinations.
In addition, various embodiments of the present invention can be combined randomly, as long as its
Without prejudice to the thought of the present invention, it should equally be considered as content disclosed in this invention.