CN106318522B - A kind of gas engine lubricant oil composite and preparation method thereof - Google Patents

A kind of gas engine lubricant oil composite and preparation method thereof Download PDF

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CN106318522B
CN106318522B CN201510333110.4A CN201510333110A CN106318522B CN 106318522 B CN106318522 B CN 106318522B CN 201510333110 A CN201510333110 A CN 201510333110A CN 106318522 B CN106318522 B CN 106318522B
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lubricant oil
oil composite
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CN106318522A (en
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谢欣
陈政
张建荣
武志强
孙洪伟
段庆华
王立华
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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 discloses a kind of gas engine lubricant oil composites, on the basis of the weight of lubricant oil composite, lubricant oil composite contains following components: the lube base oil of 75-95 weight %, the antioxygen multipurpose additive of 0.01-10 weight %, the thiophenols ester type antioxidant of 0.02-8 weight %, the polyisobutylene succinic acid ester dispersing agent of 0.5-10 weight %, the mixture of the high base number naphthenate of 0.2-10 weight % and middle base number naphthenate, in terms of phosphorus≤zinc dialkyl dithiophosphate of 0.15 weight % and the Ashless friction modifiers of 0.01-5 weight %, antioxygen multipurpose additive is the compound of structure shown in formula (I).The present invention also provides the preparation methods of gas engine lubricant oil composite.Gas engine lubricant oil composite of the invention has excellent wear-resistant and antioxygenic property, can inhibit the generation of high temperature deposition object, can be widely applied to gas engine field.

Description

A kind of gas engine lubricant oil composite and preparation method thereof
Technical field
The present invention relates to lubricating oil fields, and in particular, to a kind of gas engine lubricating oil containing special additive Composition and preparation method thereof.
Background technique
Low emission, low fuel expense and the reasonable fuel source configuration feature of compressed natural gas, as automobile engine Fuel is paid more and more attention in the world, has also pushed the development of automobile with compressed natural gas, and technology development also reaches its maturity.By The compressed natural gas repacked into using gasoline car/gasoline dual-purpose fuel vehicle is well received in big and medium-sized cities, development prospect Also very bright.However, the original gasoline engine oil of this kind of vehicle occurs, carbon deposit is more, greasy filth is big, the drain period shortens etc. asks Topic;Easily there is the problems such as premature wear and shortening of overhaul mileage in engine.Gasoline engine oil is in automobile compressed natural gas/gasoline dual-purpose Using producing some problems on engine fuel.From service performance, gasoline engine oil does not meet the combustion of CNG/ gasoline dual-purpose yet Expect requirement of the engine to lubricating oil.Compressed natural gas/gasoline dual purpose fuel engine use natural gas when, chamber temperature compared with High, exhaust emissions temperature height requires the high-temperature oxidation resistance of engine oil under this operating condition higher.Simultaneously because containing metal The additive of ash content easily in the hard deposit of engine components Surface Creation, causes piston and steel bushing component of engine etc. to rub Being seriously worn of portion, piston region carbon deposit increases, burns phenomena such as valve, therefore gas engine oil wants high temperature wear resistance It asks with the power parameter that gas engine is continuously improved and is continuously improved.Therefore developing novel has excellent high temperature antioxygen anti- The gas engine lubricant oil composite for grinding performance becomes the striving direction of those skilled in the art.
It mainly includes phenols and aminated compounds that the lube oil additive of antioxidation can be effectively played by, which being currently known,. Phenolic compound contains one or more and is obstructed phenol functional group, and aminated compounds then contains one or more nitrogen-atoms, these are special Different functional group can capture the free radical compounds of oxidation process generation, so that oxidation process be prevented to continue to occur.Due to The operating condition of Current mechanical equipment tends to strongly, often accelerated oxidation rate, shortens the service life of lubricating oil, therefore right More stringent requirements are proposed for the efficiency and economy of antioxidant.
United States Patent (USP) US4824601A reports diphenylamine and diisobutylene in the alkaline-earth metal catalyst of acid activation The lower alkylated amines mixture formed of (earth catalyst) effect, its anti-oxidant energy in lubricating oil and other functional fluids Power is excellent in.
United States Patent (USP) US2005230664A1 reports a kind of synthesis of the antioxidant acridan of following general formula Method, it is to be condensed preparation under acidic catalyst effect using alkylated diphenylamine and aldehydes or ketones.
Using the tert-butyl phenols that is obstructed, aldehyde, carbon disulfide and dialkylamine condensation preparationization occurs for patent CN1191340C Object is closed, which has the stronger ability for capturing free radical and peroxynitrite decomposition compound, can provide to oil oxidation stability More effectively protection, may also function as wear-resistant effect.
Patent US4225450A report it is a kind of by the tert-butyl phenols that is obstructed with Diethyldithiocarbamate the system of reacting Standby polysulfide phenolic antioxidant has preferable antioxidation and wear-resistant effect.
Summary of the invention
The purpose of the invention is to meet to the anti-oxidant, wear-resistant of gas engine lubricant oil composite and inhibit high temperature The high request for the ability that deposit generates provides a kind of gas engine lubricant oil composite and preparation method thereof.
The present inventor has found that lubricant oil composite contains the compound of structure shown in formula (I) under study for action:
And the compound and thiophenols ester type antioxidant are combined, and gas engine lubricant oil composite can be made to have excellent The good performances such as anti-oxidant and wear-resistant, can effectively inhibit the generation of high temperature deposition object.
Therefore, to achieve the goals above, on the one hand, the present invention provides a kind of gas engine lubricant oil composite, On the basis of the weight of lubricant oil composite, the lubricant oil composite contains following components: the lubrication oil base of 70-95 weight % Plinth oil, the thiophenols ester type antioxidant of the antioxygen multipurpose additive of 0.01-10 weight %, 0.02-8 weight %, 0.5-10 weight Measure the mixed of the polyisobutylene succinic acid ester dispersing agent of %, the high base number naphthenate of 0.2-10 weight % and middle base number naphthenate Close object, in terms of phosphorus≤zinc dialkyl dithiophosphate of 0.15 weight % and the Ashless friction modifiers of 0.01-5 weight %, institute State the compound that antioxygen multipurpose additive is structure shown in formula (I):
Preferably, on the basis of the weight of lubricant oil composite, the lubricant oil composite contains following components: 75-90 The lube base oil of weight %, the antioxygen multipurpose additive of 0.1-4 weight %, 0.1-3 weight % thiophenols ester type antioxygen Agent, the polyisobutylene succinic acid ester dispersing agent of 3-7 weight %, 0.8-6 weight % high base number naphthenate and middle base number cycloalkanes Ashless the rubbing of the mixture of hydrochlorate, the zinc dialkyl dithiophosphate of the weight of the 0.01-0.1 in terms of phosphorus % and 0.05-1.2 weight % Wipe modifier.
On the other hand, the present invention provides a kind of preparation method of gas engine lubricant oil composite, the method packets Include: will containing lube base oil, antioxygen multipurpose additive, thiophenols ester type antioxidant, polyisobutylene succinic acid ester dispersing agent, The original of the mixture of high base number naphthenate and middle base number naphthenate, zinc dialkyl dithiophosphate and Ashless friction modifiers Material is uniformly mixed and obtains lubricant oil composite, wherein on the basis of the weight of lubricant oil composite, the dosage of lube base oil Dosage for 70-95 weight %, antioxygen multipurpose additive is 0.01-10 weight %, the dosage of thiophenols ester type antioxidant is 0.02-8 weight %, polyisobutylene succinic acid ester dispersing agent dosage be 0.5-10 weight %, high base number naphthenate and middle alkali The dosage for being worth the mixture of naphthenate is 0.2-10 weight %, the dosage of zinc dialkyl dithiophosphate be in terms of phosphorus≤0.15 Weight %, the dosage of Ashless friction modifiers are 0.01-5 weight %, and the antioxygen multipurpose additive is structure shown in formula (I) Compound:
Preferably, on the basis of the weight of lubricant oil composite, the dosage of lube base oil is 75-90 weight %, resists The dosage of oxygen multipurpose additive is 0.1-4 weight %, the dosage of thiophenols ester type antioxidant is 0.1-3 weight %, polyisobutene The dosage of succinate dispersing agent is 3-7 weight %, the dosage of the mixture of high base number naphthenate and middle base number naphthenate For 0.8-6 weight %, the dosage of zinc dialkyl dithiophosphate is the weight % of the 0.01-0.1 in terms of phosphorus, Ashless friction modifiers Dosage is 0.05-1.2 weight %.
Gas engine lubricant oil composite of the invention has excellent abrasion resistance and antioxygenic property, can inhibit height The generation of warm deposit can be widely applied to combustion gas and start so as to avoid spark plug from blocking and engine advanced ignition Machine field.
Other features and advantages of the present invention will the following detailed description will be given in the detailed implementation section.
Detailed description of the invention
Fig. 1 is the reaction equation of (a) the step of preparing antioxygen multipurpose additive.
Fig. 2 is the reaction equation of (b) the step of preparing antioxygen multipurpose additive.
Fig. 3 is the reaction equation of (c) the step of preparing antioxygen multipurpose additive.
Fig. 4 is the hydrogen spectrum spectrogram of the antioxygen multipurpose additive of preparation example preparation.
Fig. 5 is the carbon spectrum spectrogram of the antioxygen multipurpose additive of preparation example preparation.
Fig. 6 is the mass spectrogram of the antioxygen multipurpose additive of preparation example preparation.
Specific embodiment
Detailed description of the preferred embodiments below.It should be understood that described herein specific Embodiment is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
On the one hand, the present invention provides a kind of gas engine lubricant oil composites, are with the weight of lubricant oil composite Benchmark, lubricant oil composite contain following components: lube base oil, the antioxygen of 0.01-10 weight % of 70-95 weight % is more Imitate additive, the thiophenols ester type antioxidant of 0.02-8 weight %, 0.5-10 weight % polyisobutylene succinic acid ester dispersing agent, The mixture of the high base number naphthenate of 0.2-10 weight % and middle base number naphthenate, in terms of phosphorus≤dioxane of 0.15 weight % The Ashless friction modifiers of base zinc dithiophosphate and 0.01-5 weight %, antioxygen multipurpose additive are structure shown in formula (I) Compound:
In the present invention, on the basis of the weight of lubricant oil composite, the content of lube base oil is preferably 75-90 weight Measure %;The content of antioxygen multipurpose additive is preferably 0.02-5 weight %, more preferably 0.1-4 weight %;Thiophenols ester type is anti- The content of oxygen agent is preferably 0.05-4 weight %, more preferably 0.1-3 weight %;The content of polyisobutylene succinic acid ester dispersing agent Preferably 1.5-8 weight %, more preferably 3-7 weight %;The mixture of high base number naphthenate and middle base number naphthenate Content is preferably 0.5-8 weight %, more preferably 0.8-6 weight %;The content of zinc dialkyl dithiophosphate is preferred in terms of phosphorus For 0.01-0.1 weight %;The content of Ashless friction modifiers is preferably 0.02-2 weight %, more preferably 0.05-1.2 weight Measure %.
The present invention is directed to tie by the compound containing structure shown in formula (I) in lubricant oil composite, and shown in formula (I) The compound of structure and thiophenols ester type antioxidant are combined and realize goal of the invention, though lubricant oil composite have it is excellent wear-resistant With the performances such as anti-oxidant.Therefore, it for the selection of conventional constituents each in lubricant oil composite, does not limit specifically.
In the present invention, lube base oil can be lube base oil commonly used in the art, such as can be mine Object lubricating oil and/or synthetic lubricant fluid.
Mineral lubricating oil in viscosity can from light fraction mineral oil to heavy distillat mineral oil, including saxol and plus That hydrogen refines, the processed alkane of solvent, cycloalkanes and mixing par-affinic-naphthenic types mineral lubricating oil, are generally divided into I, II, Group III Base oil, common trade names include I class 150SN, 600SN, II class 100N, 150N, 350N etc..
Synthetic lubricant fluid may include polymerization hydrocarbon ils, alkyl benzene and its derivative, polymerization hydrocarbon ils specific example include but It is not limited to polybutene, polypropylene, propylene-isobutylene copolymers, the polybutene of chlorination, poly- (1- hexene), poly- (1- octene), gathers (1- decene), common trade names include PAO4, PAO6, PAO8, PAO10 etc., alkyl benzene and its derivative specific example Including but not limited to detergent alkylate, Tetradecylbenzene, dinonyl benzene, two (2- ethylhexyl) benzene, alkyl benzene derivate packet Include alkylated diphenyl ether and alkylated diphenyl sulfide and its derivative, analog and homologue etc..
Another suitable type of synthetic lubricant fluid can be Esters oil, including dicarboxylic acids (such as phthalic acid, succinic acid, alkane Base succinic acid and alkenyl succinic acid, maleic acid, azelaic acid, suberic acid, decanedioic acid, fumaric acid, adipic acid, linoleic acid dimerization Object, malonic acid, alkyl malonic acid, alkenyl malonic) with various alcohol (such as butanol, hexanol, dodecyl alcohol, 2- ethylhexyl alcohol, Ethylene glycol, propylene glycol) ester or complex ester that condensation reaction generates occurs.The specific example of these esters includes but is not limited to adipic acid Dibutyl ester, decanedioic acid two (2- ethylhexyl) ester, the just own ester of fumaric acid acid two, dioctyl sebacate, azelaic acid two are different pungent Ester, two different decayl esters of azelaic acid, dioctyl phthalate, didecyl phthalate, decanedioic acid two (larane base) ester, linoleic acid 2- ethylhexyl diester of dimer etc..
Another suitable type of synthetic lubricant fluid can be for fischer tropsch process synthetic hydrocarbon oil and to this synthetic hydrocarbon oil by adding Hydrogen isomery such as is hydrocracked, dewaxes at the lube base oil that process obtain.
In the present invention, lube base oil preferred viscosities index is greater than 80, saturated hydrocarbon content and is greater than 90 weight %, sulfur content Less than the lube base oil of 0.03 weight %.
In the present invention, thiophenols ester type antioxidant can be thiophenols ester type antioxidant commonly used in the art, such as can be with For thiodipropionic acid bis-dodecanol ester (DLTDP), thio-2 acid double octadecyl esters (DSTDP), 2,5- dimercapto -1,3,4- thiophene two Azoles (DMTD) and 2, at least one of 2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionate], preferably 2,2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionate], such as the production of Sichuan Yong Ye Chemical Co., Ltd. Antioxidant 1035, the IRGANOX L115 etc. of BASF Aktiengesellschaft's production.
In the present invention, the number-average molecular weight of polyisobutene part is preferably 800- in polyisobutylene succinic acid ester dispersing agent 4000, more preferably 900-3000, further preferably 1000-2400.Polyisobutylene succinic acid ester dispersing agent can for example select The LZ936 etc. produced with Lubrizol Corp..
In the present invention, high base number naphthenate is preferably the overbased calcium alkyl-salicylate that base number is 260-400mgKOH/g, in Base number naphthenate is preferably the middle base number calcium naphthenate that base number is 150-250mgKOH/g, high base number naphthenate and middle base number The weight ratio of naphthenate is preferably 0.1-12:1, more preferably 0.6-4:1.High base number naphthenate and middle base number naphthenate Mixture T112, T113, the T114 etc. that can for example select Dushanzi petro-chemical corporation to produce.
In the present invention, the alkyl in zinc dialkyl dithiophosphate is preferably the alkyl of C2-C12, more preferably C2-C8's Alkyl, further preferably ethyl, n-propyl, isopropyl, normal-butyl, isobutyl group, sec-butyl, n-pentyl, isopentyl, just oneself Base, isohesyl, n-octyl, iso-octyl, 2- ethylhexyl, cyclohexyl or methylcyclopentyl.Zinc dialkyl dithiophosphate can be with T202, the T203 for selecting WUXI SOUTH PETROLEUM ADDITIVE Co., LTD. to produce, the primary of the production of Jinzhou Petrochemical Company additive factory Alkyl T202, primary alkyl T203, brothers alkyl T204, secondary alkyl T205, LZ1371, LZ1375 of Lubrizol Corp.'s production, profit C9417, C9425, C9426 of Ying Lian company production, Hitec7169, Hitec1656 etc. of Afton Chemical Corp.'s production.
In the present invention, Ashless friction modifiers are preferably selected from polyol esters of fatty acids, aliphatic amine and aliphatic amide One or more, the more preferably mixture of polyol esters of fatty acids and aliphatic amide, polyol esters of fatty acids and fat The weight ratio of race's amide is preferably 0.5-3:1, wherein aliphatic alkyl be preferably saturation of the carbon atom number between 6-60 or The saturation or unsaturated alkyl of unsaturated alkyl, more preferably carbon atom number between 10-50.
The polyol esters of fatty acids is preferably selected from fatty glyceride, fatty acid pentaerythritol ester, fatty acid ethylene glycol The compounds such as ester, fatty acid succinate, fatty acid ethanolamide amine ester, fatty acid diethanolamine ester, fatty acid triethanolamine ester At least one of monoesters, dibasic acid esters and polyester are more preferably selected from glyceryl monooleate, double oleins, stearic acid single cropping penta At least one of four alcohol esters, lauric acid/dodecanoic acid diethylene glycol dilaurate, oleic acid diethanol amine monoesters and triethanolamine oleate monoesters;The rouge Fat race amine is preferably selected from alkyl and monoamine or polyamine, alkoxylated alkyl is replaced to replace monoamine or polyamine and alkyl ether The butter fat ether amines of at least one of amine etc., the more preferably tallow amine of ethoxylation and/or ethoxylation;It is described Aliphatic amide is preferably selected from least one of oleamide, coconut oleoyl amine and oleic acid diethyl amide etc..Ashless friction changes F10, F20 etc. of BASF Aktiengesellschaft can be for example selected into agent.
Lubricant oil composite of the invention can also contain at least one in antirust agent, pour-point depressant, tackifier and anti-foaming agent Kind.Antirust agent can be selected from imidazoles and/or alkenyl succinic acid esters, preferably 4,5- glyoxalidine, alkenyl imidazoline fourth two At least one of hydrochlorate and alkenyl succinic acid ester, such as Jinzhou Kangtai Lube Additive Co., Ltd. can be selected to produce T746,T703,T747.The dialkyl group that pour-point depressant can be C8-C18 selected from poly alpha olefin, vinyl acetate copolymer and alkyl At least one of fumarate, poly- alkylmethacrylate, alkylnaphthalene, such as Wuxi south petroleum additive can be selected V385, Luo Mankesi VISCOPLEX1-248 of T803, Run Yinglian company of company etc..Tackifier can be total selected from ethylene, propylene At least one of polymers, polymethyl methacrylate and hydrogenated styrene isoprene copolymer, for example, can select T601, SV260, Lz7065 etc..Anti-foaming agent can select polysiloxane type anti-foaming agent, such as can be silicone oil and/or polydimethylsiloxanes Alkane.For antirust agent, pour-point depressant, tackifier and anti-foaming agent content without particular/special requirement, can be the content of this field routine, this Known to those skilled in the art, details are not described herein.
In the present invention, the preparation method of the compound of structure shown in formula (I) is preferably included:
(a) 2,6- DI-tert-butylphenol compounds, formaldehyde and benzene are subjected to condensation reaction, generate intermediate M shown in formula (II),
(b) the intermediate M that step (a) obtains is contacted with bromide reagent and carries out bromo-reaction, generated shown in formula (III) Bromination product,
(c) bromination product for obtaining step (b) is contacted with formula (IV) compound represented carries out coupling reaction, production (I) antioxidant shown in,
In step (a) of the present invention, the condition of condensation reaction is preferably included: 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 reacting 0.5-1.5h at -20-0 DEG C to carry out stable reaction 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, more preferably methanol and/or acetonitrile, are 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 purer intermediate M, goes back in order to obtain in step (a) of the present invention It needing to post-process the system after reaction, the mode of post-processing may include that 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 methylene chloride) of 1-10 times of volume, uses distilled water and saturated common salt water washing respectively, then The desiccant such as anhydrous calcium chloride or anhydrous sodium sulfate are added at 15-30 DEG C, keep 10-60min.It is filtered to remove desiccant 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 is preferably included: under an inert atmosphere, in the second solvent, In the presence of two catalyst, under the conditions of being protected from light, the intermediate M that step (a) obtains is reacted at 15-30 DEG C with bromide reagent 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, methylene chloride, 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 using NBS, and purpose by way of example only is not construed as limiting the scope of the present invention.
In step (b) of the present invention, other than generating bromination product shown in formula (III), there are also the bromos at micro ortho position to produce Object generates, and the bromination product of meta position does not generate, 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 may include washing, drying, solvent, example be 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 desiccant, 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 is preferably included: under an inert atmosphere, in third solvent, In the presence of three catalyst, the bromination product that step (b) obtains is reacted at 80-100 DEG C with formula (IV) compound represented 4-8h。
" inert atmosphere " is as previously mentioned, details are not described herein.
In the present invention, in order to carry out stable reaction, it is preferably gradually heated to 80-100 DEG C, it is then anti-at 80-100 DEG C Answer 4-8h.
In the present invention, third solvent is preferably selected from least one of methylene chloride, chloroform, toluene and tetrahydrofuran, more Preferably methylene chloride.
In the present invention, third catalyst preferably includes palladium salt, ligand and alkali.Palladium salt is preferably selected from palladium acetate and/or palladium-two BENZYLIDENE ACETONE complex compound [Pd2(dba)3];Ligand is preferably selected from tri-tert-butylphosphine, dinaphthol (BINAP) and bis- (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, the dosage of bromination product and formula (IV) compound represented that step (b) obtains is 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, the 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 acetate, purpose by way of example only, not to this The range 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, for the method for the present invention it is also preferable to include post-processing to the system after reaction, the mode of post-processing may include filtering, solvent Washing, drying, solvent is removed under reduced pressure in dilution, for example, the filtered filtrate of system after reaction to be poured into the second of 1-10 times of volume It in acetoacetic ester (or methylene chloride), is then washed with distilled water, anhydrous calcium chloride or anhydrous sulphur is then added at 15-30 DEG C The desiccant such as sour sodium keep 10-60min.After being filtered to remove desiccant, solvent is removed at 0.01-0.05MPa, 40-60 DEG C, To obtain 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 third The amount of agent can be the solvent usage 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, the present invention is directed to the compound by containing structure shown in formula (I) in lubricant oil composite, and formula (I) compound and thiophenols ester type antioxidant of structure shown in are combined and realize goal of the invention, even if lubricant oil composite has The excellent performances such as wear-resistant and anti-oxidant, inhibit the generation of high temperature deposition object.Therefore, for the preparation method of lubricant oil composite Without particular/special requirement, method commonly used in the art can be used, for example, second aspect, the present invention also provides a kind of combustion gas The preparation method of engine oil composition, this method comprises: lube base oil, antioxygen multipurpose additive, sulphur will be contained For phenolic ester type antioxidant, polyisobutylene succinic acid ester dispersing agent, high base number naphthenate and middle base number naphthenate mixture, The raw material of zinc dialkyl dithiophosphate and Ashless friction modifiers is uniformly mixed and obtains lubricant oil composite, wherein with lubrication On the basis of the weight of fluid composition, the dosage of lube base oil is 70-95 weight %, the dosage of antioxygen multipurpose additive is 0.01-10 weight %, thiophenols ester type antioxidant dosage be 0.02-8 weight %, polyisobutylene succinic acid ester dispersing agent use Measuring is 0.5-10 weight %, and the dosage of the mixture of high base number naphthenate and middle base number naphthenate is 0.2-10 weight %, The dosage of zinc dialkyl dithiophosphate be in terms of phosphorus≤0.15 weight %, the dosages of Ashless friction modifiers is that 0.01-5 is weighed % is measured, antioxygen multipurpose additive is 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 oil composite, the dosage of lube base oil is 75-90 weight %, the dosage of antioxygen multipurpose additive are 0.02-5 weight %, more preferably 0.1-4 weight %, thiophenols ester type The dosage of antioxidant is 0.05-4 weight %, and the dosage of more preferably 0.1-3 weight %, polyisobutylene succinic acid ester dispersing agent are The dosage of the mixture of 1.5-8 weight %, more preferably 3-7 weight %, high base number naphthenate and middle base number naphthenate is 0.5-8 weight %, more preferably 0.8-6 weight %, the dosage of zinc dialkyl dithiophosphate are the weight of the 0.01-0.1 in terms of phosphorus % is measured, the dosage of Ashless friction modifiers is 0.02-2 weight %, more preferably 0.05-1.2 weight %.
As previously mentioned, raw material can also be containing in antirust agent, pour-point depressant, tackifier and anti-foaming agent in the method for the present invention It is at least one.
In the method for the present invention, for mixed mode without particular/special requirement, such as each original of lube base oil can will be removed Material component is added separately in lube base oil, can also will be mixed and made into concentrate again except each component of lube base oil It is added in lube base oil.
In the method for the present invention, mixed condition is preferably included: temperature is 40-90 DEG C, time 1-6h.
Lube base oil, antioxygen multipurpose additive, thiophenols ester type antioxidant, polyisobutylene succinic acid ester dispersing agent, The mixture of high base number naphthenate and middle base number naphthenate, zinc dialkyl dithiophosphate, Ashless friction modifiers, antirust Agent, pour-point depressant, tackifier and anti-foaming agent are as previously mentioned, details are not described herein.
Embodiment
The present invention is further illustrated for embodiment below, but is not intended to limit the present invention.
In the following Examples and Comparative Examples:
The physico-chemical analysis method of product: constituent content is measured by inductively coupled plasma body ion emission spectroscopy method.
Structure characterization methods: nuclear magnetic resonance method (1H hydrogen spectrum,13C carbon spectrum), high resolution mass spectrum.
Preparation example
It is filled with nitrogen protection in the 500mL flask with electromagnetic agitation sub (mixing speed 200rpm), 150mL is added Methanol and 0.01mol acetic acid, after being fully cooled in ice-water bath, be then respectively adding 2, the 6- di-tert-butyl of 0.1mol Phenol, the formaldehyde of 0.2mol and the benzene of 0.3mol.Reaction moves back ice-water bath in 1 hour, and 75 DEG C are heated to after rising to 25 DEG C and is persistently returned Stream stops reaction after 2 hours, the system after reaction is steamed solvent at 0.03MPa, 50 DEG C, and 250mL acetic acid second is then added Ester, and be transferred in separatory funnel, 100mL distilled water (twice) and 50mL saturated common salt water washing are used respectively, and it is anhydrous that 10g is added Calcium chloride dry 20min, filtered filtrate at 25 DEG C are evaporated off solvent at 40 DEG C, 0.03MPa, obtain midbody product M1。
It is filled with nitrogen protection in the 500mL flask with electromagnetic agitation sub (mixing speed 200rpm), 150mL is added Dry tetrahydrofuran, then dissolve in midbody product M1, and the ammonium nitrate of 0.05mol is added, under the conditions of being protected from light slowly plus Enter 0.1mol brominated reagent NBS.It is stirred to react 1.5h at 25 DEG C, is then quenched with saturated salt solution, is then distilled with 100mL Water (twice) washing, and 10g anhydrous sodium sulfate dry 20min at 25 DEG C is added.Filtered filtrate is in 40 DEG C, 0.03MPa Under solvent is evaporated off, obtain bromination product.
It is filled with nitrogen protection in the 500mL flask with electromagnetic agitation sub (mixing speed 200rpm), 150mL is added Methylene chloride as solvent, be separately added into above-mentioned bromination product and the benzotriazole compound of 0.12mol, then be added The tri-tert-butylphosphine of 0.02mol, the sodium tert-butoxide of 0.02mol and the Pd (OAc) of 0.005mol2.90 DEG C are gradually heated to, is continued Stir 6h.Then 250mL ethyl acetate is added in the filtered filtrate of system after reaction, and be transferred in separatory funnel, used 100mL distilled water (twice) washing, and 10g anhydrous sodium sulfate dry 20min at 25 DEG C is added.Filtered filtrate is 40 DEG C, solvent is evaporated off under 0.03MPa, obtain final product S1.
The physico-chemical analysis data of S1 are as follows: nitrogen content, and 11.2%.
S1 is subjected to structural characterization, respectively obtain hydrogen spectrum, carbon spectrum and high resolution mass spec spectrogram, see respectively Fig. 4, Fig. 5 and Fig. 6.
It can be seen that S1 with knot shown in formula (I) from the physico-chemical analysis data of above-mentioned preparation example, Fig. 4, Fig. 5 and Fig. 6 Structure.
Embodiment 1
The present embodiment is for illustrating lubricant oil composite and preparation method thereof of the invention.
By the S1 of 0.1 parts by weight, 2,2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) propionic acid of 3 parts by weight Ethyl ester], the polyisobutylene succinic acid ester dispersing agent of 7 parts by weight (number-average molecular weight of polyisobutene part is 2400), 2 parts by weight Overbased calcium alkyl-salicylate (base number 260mgKOH/g), 1 parts by weight middle base number calcium naphthenate (base number 200mgKOH/g), Two isohesyl zinc dithiophosphates of 0.12 parts by weight, the glyceryl monooleate of 0.03 parts by weight, 0.02 parts by weight oleic acid acyl Amine, the pour-point depressant VISCOPLEX1-248 (be purchased from U.S. Luo Mankesi Allied Corp. (US) Law Department P.O. Box 2245R. Morristown, NJ 07960-2245, U.S.) of 0.3 parts by weight and 6.5 parts by weight Tackifier SV260 is added to 600SN lube base oil (viscosity index (VI) 87, the saturated hydrocarbon content 92 of 79.93 parts by weight Weight %, sulfur content are 0.02 weight %) in, 3h is stirred at 60 DEG C, is uniformly mixed and obtains lubricant oil composite A1.
Embodiment 2
The present embodiment is for illustrating lubricant oil composite and preparation method thereof of the invention.
By the S1 of 0.5 parts by weight, the 2,2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) third of 0.5 parts by weight Acetoacetic ester], the polyisobutylene succinic acid ester dispersing agent of 3.5 parts by weight (number-average molecular weight of polyisobutene part is 1300), 0.5 The overbased calcium alkyl-salicylates (base number 300mgKOH/g) of parts by weight, 0.4 parts by weight middle base number calcium naphthenate (base number is 150mgKOH/g), the isobutyl group n-octyl zinc dithiophosphate, the isopropyl hexyl two of 0.4 parts by weight of 0.2 parts by weight are thio Trbasic zinc phosphate, the stearic acid monopentaerythritol ester of 0.1 parts by weight, the oleic acid diethyl amide of 0.2 parts by weight, 0.3 parts by weight drop The tackifier SV260 of solidifying agent VISCOPLEX1-248 (being purchased from U.S. Luo Mankesi Allied Corp. (US) Law Department P.O. Box 2245R. Morristown, NJ 07960-2245, U.S.) and 6.5 parts by weight, is added To the Group III 150N base oil (viscosity index (VI) 128) of 72 parts by weight and the Group III 350N base oil (viscosity of 14.9 parts by weight Index is to stir 6h at 40 DEG C in mixed lubrication oil base oil 126), is uniformly mixed and obtains lubricant oil composite A2.
Embodiment 3
The present embodiment is for illustrating lubricant oil composite and preparation method thereof of the invention.
By the S1 of 4 parts by weight, 2,2'- thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) propionic acid of 0.1 parts by weight Ethyl ester], the polyisobutylene succinic acid ester dispersing agent of 5 parts by weight (number-average molecular weight of polyisobutene part is 1000), 4.8 weight Part overbased calcium alkyl-salicylate (base number 400mgKOH/g), 1.2 parts by weight middle base number calcium naphthenate (base number is 250mgKOH/g), two isohesyl zinc dithiophosphates of 1.1 parts by weight, double oleins of 0.9 parts by weight, 0.3 parts by weight Coconut oleoyl amine, 0.3 parts by weight pour-point depressant VISCOPLEX1-248 (be purchased from U.S. Luo Mankesi Allied Corp. (US) Law Department P.O. Box 2245R. Morristown, NJ 07960-2245, U.S.) and 6.5 The tackifier SV260 of parts by weight, being added to the 100N lube base oils of 75.8 parts by weight, (viscosity index (VI) 112, saturated hydrocarbons contains Amount is 96 weight %) in, 1h is stirred at 90 DEG C, is uniformly mixed and obtains lubricant oil composite A3.
Comparative example 1
Lubricant oil composite is prepared according to the method for embodiment 2, unlike, S1 is replaced with etc. the 2,2'- of parts by weight Thiobis [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionate], obtains lubricant oil composite D1.
Comparative example 2
Lubricant oil composite is prepared according to the method for embodiment 2, unlike, by 2,2'- thiobis [3- (3,5- bis- uncles Butyl -4- hydroxy phenyl) ethyl propionate] S1 that the parts by weight such as replaces with, obtain lubricant oil composite D2.
Comparative example 3
Lubricant oil composite is prepared according to the method for embodiment 2, unlike, by S1 and 2,2'- thiobis [3- (3,5- Di-tert-butyl-hydroxy phenyl) ethyl propionate] zinc dibutyl dithiocarbamate that the parts by weight such as replaces with, it is lubricated Fluid composition D3.
Comparative example 4
Lubricant oil composite is prepared according to the method for embodiment 2, unlike, by S1 and 2,2'- thiobis [3- (3,5- Di-tert-butyl-hydroxy phenyl) ethyl propionate] the trimethylphenyl zinc phosphite that the parts by weight such as replaces with, obtain lubricating oil composition Object D4.
Comparative example 5
Lubricant oil composite is prepared according to the method for embodiment 2, unlike, by S1 and 2,2'- thiobis [3- (3,5- Di-tert-butyl-hydroxy phenyl) ethyl propionate] the fourth octyl diphenylamine that the parts by weight such as replaces with, obtain lubricant oil composite D5.
Test case
Lubricant oil composite A1-A3, D1-D5 are tested as follows respectively:
The measurement of initial oxidation temperature is carried out using TA5000-DSC2910 differential thermal analyzer;
The measurement of oxidation induction period is carried out using high pressure differential scanning amount method (PDSC);
Deposit production quantity is measured using crankcase QZX experiment method: QZX experiment instrument is added in 300mL oil sample, Heating and keeping oil temperature is 130 DEG C, and aluminium sheet temperature is 290 DEG C, to the continuous spilled oil 6h of aluminium sheet, is generated on weighing aluminium sheet after test Jiao Liang, as deposit production quantity.
Wear scar diameter is measured using SH/T 0189.It the results are shown in Table 1.
Table 1
A1 A2 A3 D1 D2 D3 D4 D5
Initial oxidation temperature, DEG C 242 231 258 209 220 208 191 196
Oxidation induction period, min 42.5 48.8 73.1 30.4 39.5 31.5 19.6 24.7
Deposit production quantity, mg 16.3 18.2 11.2 37.4 22.8 40.3 68.5 66.2
Wear scar diameter d60 40, mm 0.51 0.48 0.40 0.72 0.55 0.71 0.60 0.72
It will be understood by those skilled in the art that initial oxidation temperature is higher, the thermal stability of lubricating oil is better;Oxidation Induction period is longer, and the antioxygenic property of lubricating oil is better;Deposit production quantity is higher, and lubricating oil inhibits high temperature deposition object to generate Ability is poorer;Wear scar diameter is smaller, and the wear resistance of lubricating oil is better.
A2 is compared with D1-D5 respectively as can be seen that lubricant oil composite of the invention has better thermostabilization Property, inoxidizability and abrasion resistance, there is the ability for preferably high temperature deposition object being inhibited to generate.
Gas engine lubricant oil composite of the invention has excellent abrasion resistance and antioxygenic property, can inhibit height The generation of warm deposit can be widely applied to combustion gas and start so as to avoid spark plug from blocking and engine advanced ignition Machine field.
It is described the prefered embodiments of the present invention in detail above in conjunction with attached drawing, still, the present invention is not limited to above-mentioned realities The detail in mode is applied, within the scope of the technical concept of the present invention, a variety of letters can be carried out to technical solution of the present invention Monotropic type, these simple variants all belong to the scope of protection of the present invention.
It is further to note that specific technical features described in the above specific embodiments, in not lance In the case where shield, can be combined in any appropriate way, in order to avoid unnecessary repetition, the present invention to it is various can No further explanation will be given for the combination of energy.
In addition, various embodiments of the present invention can be combined randomly, as long as it is without prejudice to originally The thought of invention, it should also be regarded as the disclosure of the present invention.

Claims (28)

1. a kind of gas engine lubricant oil composite, which is characterized in that on the basis of the weight of lubricant oil composite, the profit Sliding oil composition contains following components: the antioxygen multiple-effect addition of the lube base oil, 0.01-10 weight % of 70-95 weight % Agent, the thiophenols ester type antioxidant of 0.02-8 weight %, 0.5-10 weight % polyisobutylene succinic acid ester dispersing agent, 0.2-10 The mixture of the high base number naphthenate of weight % and middle base number naphthenate, in terms of phosphorus≤dialkyl disulfides of 0.15 weight % For the Ashless friction modifiers of trbasic zinc phosphate and 0.01-5 weight %, the antioxygen multipurpose additive is the change of structure shown in formula (I) Close object:
2. lubricant oil composite according to claim 1, wherein on the basis of the weight of lubricant oil composite, the profit Sliding oil composition contains following components: the lube base oil of 75-90 weight %, 0.1-4 weight % antioxygen multipurpose additive, The thiophenols ester type antioxidant of 0.1-3 weight %, the polyisobutylene succinic acid ester dispersing agent of 3-7 weight %, 0.8-6 weight % The dialkyl dithiophosphoric acid of the mixture of high base number naphthenate and middle base number naphthenate, the weight of the 0.01-0.1 in terms of phosphorus % The Ashless friction modifiers of zinc and 0.05-1.2 weight %.
3. lubricant oil composite according to claim 1 or 2, wherein the lube base oil be mineral lubricating oil and/ Or synthetic lubricant fluid.
4. lubricant oil composite according to claim 1 or 2, wherein the thiophenols ester type antioxidant is that 2,2'- is thio Bis- [3- (3,5- di-tert-butyl-hydroxy phenyl) ethyl propionates].
5. lubricant oil composite according to claim 1 or 2, wherein gather in the polyisobutylene succinic acid ester dispersing agent The number-average molecular weight of isobutene part is 800-4000.
6. lubricant oil composite according to claim 5, wherein poly- isobutyl in the polyisobutylene succinic acid ester dispersing agent The number-average molecular weight of alkene part is 900-3000.
7. lubricant oil composite according to claim 6, wherein poly- isobutyl in the polyisobutylene succinic acid ester dispersing agent The number-average molecular weight of alkene part is 1000-2400.
8. lubricant oil composite according to claim 1 or 2, wherein it is 260- that the high base number naphthenate, which is base number, The overbased calcium alkyl-salicylate of 400mgKOH/g, the middle base number naphthenate are the middle base number ring that base number is 150-250mgKOH/g The weight ratio of alkanoic acid calcium, the high base number naphthenate and the middle base number naphthenate is 0.1-12:1.
9. lubricant oil composite according to claim 8, wherein the high base number naphthenate and the middle base number cycloalkanes The weight ratio of hydrochlorate is 0.6-4:1.
10. lubricant oil composite according to claim 1 or 2, wherein the alkyl in the zinc dialkyl dithiophosphate For the alkyl of C2-C12.
11. lubricant oil composite according to claim 10, wherein the alkyl in the zinc dialkyl dithiophosphate is The alkyl of C2-C8.
12. lubricant oil composite according to claim 11, wherein the alkyl in the zinc dialkyl dithiophosphate is Ethyl, n-propyl, isopropyl, normal-butyl, isobutyl group, sec-butyl, n-pentyl, isopentyl, n-hexyl, isohesyl, n-octyl or 2- ethylhexyl.
13. lubricant oil composite according to claim 1 or 2, wherein it is more that the Ashless friction modifiers are selected from fatty acid One of first alcohol ester, aliphatic amine and aliphatic amide are a variety of, the weight ratio of polyol esters of fatty acids and aliphatic amide For 0.5-3:1, the carbon atom number of polyol esters of fatty acids, aliphatic amine and aliphatic amide is 6-60.
14. lubricant oil composite according to claim 13, wherein the Ashless friction modifiers are fatty polyol The mixture of ester and aliphatic amide.
15. lubricant oil composite according to claim 13, wherein the polyol esters of fatty acids, aliphatic amine and rouge The carbon atom number of fat race amide is 10-50.
16. lubricant oil composite according to claim 13, wherein the polyol esters of fatty acids is selected from fatty acid glycerine At least one of ester, fatty acid pentaerythritol ester, the monoesters of ethylene glycol fatty acid, dibasic acid esters and polyester, the aliphatic amine In monoamine or polyamine and alkyl ether amine selected from monoamine or polyamine, the substitution of alkoxylated alkyl that alkyl replaces At least one, the aliphatic amide are selected from least one of oleamide, coconut oleoyl amine and oleic acid diethyl amide.
17. lubricant oil composite according to claim 16, wherein the polyol esters of fatty acids is selected from single oleic At least one of ester, double oleins, stearic acid monopentaerythritol ester and lauric acid/dodecanoic acid diethylene glycol dilaurate;The aliphatic amine For the tallow amine of ethoxylation and/or the butter fat ether amines of ethoxylation.
18. lubricant oil composite according to claim 1 or 2, wherein the lubricant oil composite also contain antirust agent, At least one of pour-point depressant, tackifier and anti-foaming agent.
19. lubricant oil composite according to claim 18, wherein the antirust agent is selected from imidazoles and/or allyl butyrate Two esters of gallic acid.
20. lubricant oil composite according to claim 19, wherein the antirust agent is selected from 4,5- glyoxalidine, alkenyl At least one of imidazoline succinate and alkenyl succinic acid ester.
21. lubricant oil composite according to claim 18, wherein the pour-point depressant is selected from poly alpha olefin, alkyl C8- At least one of the dialkyl fumarate of C18, poly- alkylmethacrylate, alkylnaphthalene.
22. lubricant oil composite according to claim 18, wherein the tackifier is ethylene propylene copolymer, poly- first At least one of base methyl acrylate and hydrogenated styrene isoprene copolymer.
23. lubricant oil composite according to claim 18, wherein the anti-foaming agent is polysiloxane type anti-foaming agent.
24. lubricant oil composite according to claim 23, wherein the anti-foaming agent is silicone oil.
25. lubricant oil composite according to claim 23, wherein the anti-foaming agent is dimethyl silicone polymer.
26. a kind of preparation method of gas engine lubricant oil composite, which is characterized in that the described method includes: profit will be contained Lubricant base oil, antioxygen multipurpose additive, thiophenols ester type antioxidant, polyisobutylene succinic acid ester dispersing agent, high base number cycloalkanes The raw material of the mixture of hydrochlorate and middle base number naphthenate, zinc dialkyl dithiophosphate and Ashless friction modifiers is uniformly mixed Obtain lubricant oil composite, wherein on the basis of the weight of lubricant oil composite, the dosage of lube base oil is 70-95 weight Measure %, the dosage of antioxygen multipurpose additive is 0.01-10 weight %, the dosage of thiophenols ester type antioxidant is 0.02-8 weight Measure %, the dosage of polyisobutylene succinic acid ester dispersing agent is 0.5-10 weight %, high base number naphthenate and middle base number aphthenic acids The dosage of the mixture of salt is 0.2-10 weight %, the dosage of zinc dialkyl dithiophosphate be in terms of phosphorus≤0.15 weight %, The dosage of Ashless friction modifiers is 0.01-5 weight %, and the antioxygen multipurpose additive is the compound of structure shown in formula (I):
27. according to the method for claim 26, wherein on the basis of the weight of lubricant oil composite, lube base oil Dosage be 75-90 weight %, the dosage that the dosage of antioxygen multipurpose additive is 0.1-4 weight %, thiophenols ester type antioxidant Dosage for 0.1-3 weight %, polyisobutylene succinic acid ester dispersing agent is 3-7 weight %, high base number naphthenate and middle base number The dosage of the mixture of naphthenate is 0.8-6 weight %, and the dosage of zinc dialkyl dithiophosphate is the 0.01-0.1 in terms of phosphorus Weight %, the dosage of Ashless friction modifiers are 0.05-1.2 weight %.
28. the method according to claim 26 or 27, wherein the mixed condition includes: that temperature is 40-90 DEG C, when Between be 1-6h.
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