CN105802697B - A kind of preparation method of the degradable methanol engine lubricating oil of improved plant oil base - Google Patents

A kind of preparation method of the degradable methanol engine lubricating oil of improved plant oil base Download PDF

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CN105802697B
CN105802697B CN201610176094.7A CN201610176094A CN105802697B CN 105802697 B CN105802697 B CN 105802697B CN 201610176094 A CN201610176094 A CN 201610176094A CN 105802697 B CN105802697 B CN 105802697B
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oil
parts
preparation
degradable
lubricating oil
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CN105802697A (en
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刘应才
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De Yipu Tianjin Science And Technology Ltd
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De Yi Pu (tianjin) Technology Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M101/00Lubricating compositions characterised by the base-material being a mineral or fatty oil
    • C10M101/04Fatty oil fractions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/283Esters of polyhydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/40Fatty vegetable or animal oils
    • C10M2207/401Fatty vegetable or animal oils used as base material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/06Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to carbon atoms of six-membered aromatic rings
    • C10M2215/064Di- and triaryl amines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/06Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)

Abstract

The present invention relates to a kind of preparation methods of the degradable methanol engine lubricating oil of improved plant oil base, belong to technical field of lubricating oil.Step: taking soybean oil, adds acid cation exchange resin, heating, hydrogen peroxide is added dropwise, formic acid is reacted, after reaction, it is washed, separates water layer, the distilled water of the modified soybean oil heat on upper layer is washed, water phase is discarded, then is neutralized with alkali, then is washed to pH neutrality with distilled water, after vacuum distillation removes moisture, modified vegetable oil is obtained;Modified vegetable oil, polyol ester, antioxidant, antirust agent, extreme pressure anti-wear additives and ashless system's detergent dispersant are uniformly mixed, heated, it is cooling, obtain lubricant oil composite.The lubricating oil that the present invention is prepared is suitable for methanol engine, and greasy property is good, biodegradable.

Description

A kind of preparation method of the degradable methanol engine lubricating oil of improved plant oil base
Technical field
The present invention relates to a kind of preparation methods of the degradable methanol engine lubricating oil of improved plant oil base, belong to lubrication Oil tech field.
Background technique
In automobilism engine motor oil consumption costs and less but it but influence automobile dynamic property, economy more It is important that therefore functional reliability and service life that it influences engine make according to the performance of engine, structure and combination Correctly select machine oil particularly significant with condition.The effect of engine lubrication mainly includes: 1, lubricating action: engine operation Shi Ruguo, which cannot suitably lubricate the parts to run at high speed, will occur caused by metal and intermetallic dry friction friction Heat can make the metal molten of rubbing surface make the stuck and good profit essence of parts that can make machine oil engaging friction machine within a very short time Being adhered to friction surface forming layer oil film between part and being not directly contacted with two rubbing surfaces as far as possible becomes intermetallic dry friction Fluid friction between liquid oil layer;2, cooling effect: maximum combustion temperature may be up to 2400 DEG C when engine operation, even if The mean temperature of idling speed lower combustion chamber also at 1000 DEG C or more, the part contacted with high-temperature fuel gas by heat intensive at this time It must carry out to which but otherwise to be stranded temperature excessively high and burn out for engine;3, anti-rust action: engine atmosphere in work or storage Water and the sour gas that generates of when burning can generate corrosiveness machine oil to parts and can be adsorbed on metal surface and prevent sour gas Body and water are to corrosion of metal.
It is constantly progressive, the demand of the energy is increasingly increased, energy problem is at restriction economic development with industrialized Big factors therefore substitute the research and use of the substitute fuel of petroleum, grown rapidly, currently, technically more Molding substitute fuel has: methanol, the substitute fuel that ethyl alcohol is gasoline;(such as: China's most area promotes 10% ethanol vapor Oil) dimethyl ether, the alternative fuel that monoesters is diesel oil;It can be seen that alcohol ethers have become mainstream, alcohol ethers as alternative fuel As alternative fuel, although playing certain effect to energy shortages is alleviated, certain technical problems in popularization are answered Cause enough attention.Especially alcohol ether class A fuel A is in use to the important additives in engine lubricating oil composition The decomposition of ZDDP (zinc dialkyl dithiophosphate), has seriously affected the antioxygenic property of former engine lubricating oil, has made it Oil draining period greatly shortens, and engine intake valve carbon distribution generates tendency and greatly increases, and long-term accumulated can seriously affect making for engine Use performance.
CN103897775A discloses a kind of different proportion alcohol engine oil ageing inhibitor and its preparation side Method.The present invention dredges base thiadiazoles 3~35% by N- phenyl-α naphthylamine 5~45%, 2,5-, amido borate 10~60%, is modified One group of compound additive that low alkali value calcium mahogany sulfonate 15~40%, flux oil 5~10% form.Preparation method of the invention It is: by 55~65 DEG C so far of flux oil heating, is then successively separately added into N- phenyl-α naphthylamine, 2,5- dredges base thiadiazoles, amido 45~50 DEG C of borate, modified low alkali value calcium mahogany sulfonate constant temperature stirrings are no less than 45min.CN105176637A discloses one kind Biology base methanol gasoline engine specific complex lubricating oil and preparation method thereof.The present invention is that squeeze into base oil can heating stirring Reaction kettle device in, be heated up to 75 DEG C, constant temperature stirs 1 hour;Then viscosity modified component is added, is heated up to 80 DEG C, constant temperature Stirring 30 minutes;By obtained mixture temperature drop to 75 DEG C, antioxygen antirust component, the anti-glue component of antioxygen, auxiliary antioxygen group is added Divide, metal detergent component, ashless dispersants component, extreme-pressure anti-wear component, metal anti-attrition component, anti-cream demulsification component, pour point depression component And oily components stir 20 minutes at 75 DEG C;Then anti-bubble component is added to stir 30 minutes;Finally obtained mixture is used Cutter do it is pre- shearing 1 hour after filtering, detection, settled in settling tank 24 hours to get.
But the cost of material of above-mentioned lubricating oil is high, and still has abrasion resistance when use in Alcohol engines Bad problem;And above-mentioned engine lubricating oil cannot be preferably biodegradable, will affect environment.
Summary of the invention
The object of the present invention is to provide a kind of lubricating oil applied to methanol engine, which needs to have preferable Biodegradable, which is that oil is prepared based on epoxy-modified vegetable oil.
Technical solution is as follows:
A kind of preparation method of the degradable methanol engine lubricating oil of improved plant oil base, comprises the following steps that
The preparation of modified vegetable oil: step 1 by weight, takes 100~120 parts of soybean oil, adds acid cation 1~3 part of exchanger resin, heating, be slowly added dropwise 5~10 parts of hydrogen peroxide, 3~6 parts of formic acid reacted, after reaction, carry out Washing, separates water layer, and the distilled water of the modified soybean oil heat on upper layer is washed, and discards water phase, then neutralized with alkali, then PH neutrality, which is washed to, with distilled water obtains modified vegetable oil after vacuum distillation removes moisture;
Step 2, by weight, by 30~40 parts of polyalcohol, 20~30 parts of ethanedioic acid, 20~30 parts of oleanonic acid, 3~5 parts of catalyst, 80~120 parts of organic solvent be uniformly mixed, then heat up, reacted, steam organic solvent, obtain more First alcohol ester;
Step 3, by weight, by 70~80 parts of modified vegetable oil, 5~10 parts of polyol ester, antioxidant 0.05~1 Part, 0.05~1 part of antirust agent, 0.05~1 part of extreme pressure anti-wear additives and 0.05~1 part of ashless system's detergent dispersant are uniformly mixed, and are added Heat is cooling to 70~120 DEG C, obtains lubricant oil composite.
In the step 1, heating is to make temperature to 50~60 DEG C, and the reaction time is that carry out 1~3 after being added dropwise again small When.In the step 1,50~60 DEG C of temperature of the distilled water of the heat.
In the step 2, the polyalcohol in hydroxymethyl-propane, glycerine, pentaerythrite, mannitol one Kind or several mixing.
Reaction time in the step 2 is 2~4 hours, 70~90 DEG C of reaction temperature.
The extreme pressure anti-wear additives are phosphate compounds, phosphite ester compound, sulphur phosphorus complexing agent or sulfur-bearing pole Press agent.
In the step 1, soybean oil is needed by pretreatment, and the preprocess method is as follows: taking 200mL soybean When temperature rises to 35 DEG C the ammonium hydroxide of the about 4wt% of oil volume a quarter is added, after adding in oil, heating in 20min Continue to stir 15min, then stop stirring, be warming up to 95 DEG C, keeps 1h;Reaction mixture is poured into separatory funnel, is stood Layering separates and rinses oil reservoir with boiling water after soap stock water;The oil reservoir separated is warming up to 93~97 DEG C again, in 10 minutes thereto The H of the 30wt% of oil volume 5% is added2O2, stop stirring, keep the temperature 1h at 120 DEG C;Stratification separates soap stock with separatory funnel Water;Oil reservoir, then stratification are rinsed with boiling water, water layer is removed, obtains pretreated soybean oil.
Beneficial effect
The lubricating oil that the present invention is prepared is suitable for methanol engine, and greasy property is good, biodegradable.
Specific embodiment
In the lubricant oil composite that the present invention uses, by the way that its biodegrade can be improved to soybean oil progress is epoxy-modified Speed, while can also improve greasy property.Polyol ester is basic components, and oleanonic acid, which is added, in preparation step to mention High biological degradability.
In addition, organic solvent is not particularly limited in ester rouge reaction process, hexane, hexamethylene, heptane etc. can be enumerated The alcohols such as the arene compounds such as alkanes, toluene, dimethylbenzene, methanol, ethyl alcohol, isopropanol, butanol, hexanol, cyclohexanol.Separately Outside, the ketones such as methyl ethyl ketone, methyl iso-butyl ketone (MIBK), cycloheptanone, cyclohexanone, ether, tetrahydrofuran, two according to circumstances also can be used Nitrile compounds such as the ester compounds such as the ethers such as oxinane, ethyl acetate, butyl acetate, methyl formate, acetonitrile etc..
It in the lubricant oil composite being prepared, is not damaging within the scope of the object of the invention, can be added as needed each Kind additive, such as: ashless system's detergent dispersant, antioxidant, antirust agent, metal deactivator, viscosity index improver, flow point At least one selected in depressant and defoaming agent etc..
Herein, ashless system's detergent dispersant can be enumerated, such as: succinimide class, boracic succinimide class, benzylamine Unitary or dicarboxylic acids amides etc. representated by class, boracic benzylamine class, succinic acid esters, fatty acid or succinic acid.It is ashless It is the combined amount of detergent dispersant, considers from the balance of effect and economy, on the basis of the total amount of composition, The left and right 0.01wt% or more, 5wt% or less.
As antioxidant, can be used amine antioxidant used in existing lubricating oil, phenolic antioxidant and Sulfur antioxidant.These antioxidants can be used alone or combine two or more use.It is arranged as amine antioxidant It lifts, such as: the monoalkyls hexichol amine compound such as single octyl diphenylamine, single nonyl diphenylamine;4,4 '-dibutyl diphenylamines, 4, 4 '-diamyl diphenylamines, 4,4 '-dihexyl diphenylamines, 4,4 '-diheptyl diphenylamines, 4,4 '-dioctyl diphenylamines, 4,4 '-two The dialkyl diphenylamines based compound such as nonyl diphenylamine;Tetrabutyl diphenylamines, four hexyl diphenylamines, four octyl diphenylamines, four nonyls The poly- alkyl diphenyl amine compound such as base diphenylamines;Alpha-naphthylamine, phenyl-α-naphthylamine, butyl phenyl-alpha-naphthylamine, benzyl phenyl-α- The naphthylamines systems such as naphthylamines, hexyl phenyl-α-naphthylamine, heptyl phenyl-α-naphthylamine, octyl phenyl-alpha-naphthylamine, nonyl phenyl-α-naphthylamine Compound.Phenolic antioxidant can be enumerated, such as: 2,6- di-t-butyl -4- aminomethyl phenyls, 2,6- di-t-butyl -4- ethylo benzene The monophenols based compounds, 4 such as base, octadecyl -3- (3,5- di-t-butyl -4- hydroxyphenyl) propionic ester, 4 '-di-2-ethylhexylphosphine oxides-(2, 6- DI-tert-butylphenol compounds), the hexichol phenol system compound such as 2,2 '-di-2-ethylhexylphosphine oxides-(4- ethyl -6- tert-butyl phenol).
Sulfur antioxidant can be enumerated, such as 2,6- di-t-butyl -4- (4,6- bis- (octylsulfo) -1,3,5-triazines -2- Base amino) the thio terpene hydro carbons based compound such as reactant of phenol, phosphoric sulfide and firpene, two laruyl alcohol thiodipropionates, Dialkyls dipropionates such as distearyl alcohol thiodipropionate etc..
Antirust agent can enumerate metal system sulfonate, alkenyl succinic acid ester etc..The combined amount of these antirust agent is imitated from mixing From the aspect of fruit, on the basis of total composition, about in 0.01wt% or more, 0.5wt% or less.
As metal deactivator (copper anticorrosive), can enumerate, such as: enumerate BTA system, tolyl-triazole system, thiophene two Azoles system, imidazoles system and pyrimidine compound etc..Wherein, preferred benzotriazole based compound.The combined amount of these metal deactivators, From the aspect of mixed effect, on the basis of total composition, about in 0.01wt% or more, 0.1wt% or less.
As viscosity index improver, can enumerate, such as: polymethacrylates, distributed polymethacrylates, Olefin copolymer (e.g., ethylene-propylene copolymer etc.), distributed olefin copolymer, styrene based copolymer (such as benzene second Alkene-diene copolymers, styrene-isoprene copolymer etc.) etc..The combined amount of these viscosity index improvers is imitated from mixing From the aspect of fruit, on the basis of total composition, about in 0.5wt% or more, 15wt% or less.
Flow point depressant can be enumerated: ethylene-vinyl acetate copolymer, the condensation product of chlorinated paraffin and naphthalene, chlorinated paraffin With the condensation product, polymethacrylates, alkyl styrenes of phenol etc., for instance, it may be preferable to using matter average molecular weight 50,000 with Above, 150,000 or less Zuo You polymethacrylates.The combined amount of flow point depressant is about existed on the basis of total composition 0.1wt% or more, 5wt% or less.
The preferred polymeric silicone system defoaming agent of defoaming agent, polyacrylate system defoaming agent, by mixing the polymeric silicone It is that defoaming agent etc. can effectively play defoaming.Such polymeric silicone system defoaming agent can enumerate for example organic poly- silicon oxygen Alkane is especially suitable for the fluorine-containing organopolysiloxanes such as three fluoro hydroxypropyl methyl silicone oil.The combined amount of defoaming agent, from defoaming effect with And the balance of economy considers, on the basis of the total amount of composition, about in 0.005wt% or more, 0.1wt% or less.
Biodegradable lubricant composition of the invention, because lubricity, oxidation stability and biological degradability are excellent It is different, so can suitably be applied to the use in such as methanol engine.
For the soybean oil used in following embodiment by pretreatment, the preprocess method is as follows: taking 200mL soybean When temperature rises to 35 DEG C the ammonium hydroxide of the about 4wt% of oil volume a quarter is added, after adding in oil, heating in 20min Continue to stir 15min, then stop stirring, be warming up to 95 DEG C, keeps 1h;Reaction mixture is poured into separatory funnel, is stood Layering separates and rinses oil reservoir with boiling water after soap stock water;The oil reservoir separated is warming up to 93~97 DEG C again, in 10 minutes thereto The H of the 30wt% of oil volume 5% is added2O2, stop stirring, keep the temperature 1h at 120 DEG C;Stratification separates soap stock with separatory funnel Water;Oil reservoir, then stratification are rinsed with boiling water, water layer is removed, obtains pretreated soybean oil.
Catalyst used in step 2 esterification is solid super acid catalyst SO in following embodiment4 2-/ZrO2
Embodiment 1
Step 1, the preparation of modified vegetable oil: by weight, taking 100 parts of soybean oil, adds acid cation exchange 1 part of resin, be warming up to 50 DEG C, be slowly added dropwise 5 parts of hydrogen peroxide, 3 parts of formic acid reacted, the reaction time be after being added dropwise again into It row 1 hour, after reaction, is washed, separates water layer, the modified soybean oil on upper layer carries out water with 50 DEG C of hot distilled water It washes, discards water phase, then neutralized with alkali, then be washed to pH neutrality with distilled water and be modified after vacuum distillation removes moisture Vegetable oil;
Step 2, by weight, by 30 parts of pentaerythrite, 20 parts of ethanedioic acid, 20 parts of oleanonic acid, catalyst 3~5 Part, 80 parts of organic solvent be uniformly mixed, then heat up, reacted, the reaction time is 2 hours, 70 DEG C of reaction temperature, has been steamed Solvent obtains polyol ester;
Step 3, by weight, by 70 parts of modified vegetable oil, 5 parts of polyol ester, four hexyl diphenylamines 0.05 of antioxidant Part, 0.05 part of metal system sulfonate antirust agent, 0.05 part of phosphite ester compound extreme pressure anti-wear additives and succinic acid esters are ashless It is 0.05 part of detergent dispersant to be uniformly mixed, be heated to 70 DEG C, cooling obtains lubricant oil composite.
Embodiment 2
Step 1, the preparation of modified vegetable oil: by weight, taking 120 parts of soybean oil, adds acid cation exchange 3 parts of resin, be warming up to 60 DEG C, be slowly added dropwise 10 parts of hydrogen peroxide, 6 parts of formic acid reacted, the reaction time be after being added dropwise again It carries out 3 hours, after reaction, is washed, separate water layer, the modified soybean oil on upper layer carries out water with 60 DEG C of hot distilled water It washes, discards water phase, then neutralized with alkali, then be washed to pH neutrality with distilled water and be modified after vacuum distillation removes moisture Vegetable oil;
Step 2, by weight, by 40 parts of pentaerythrite, 30 parts of ethanedioic acid, 30 parts of oleanonic acid, 5 parts of catalyst, 120 parts of organic solvent are uniformly mixed, and then heat up, are reacted, the reaction time is 4 hours, 90 DEG C of reaction temperature, is steamed organic Solvent obtains polyol ester;
Step 3, by weight, by 80 parts of modified vegetable oil, 10 parts of polyol ester, 1 part of four hexyl diphenylamines of antioxidant, 1 part of metal system sulfonate antirust agent, 1 part of phosphite ester compound extreme pressure anti-wear additives and the ashless system's cleaning dispersion of succinic acid esters 1 part of agent is uniformly mixed, and is heated to 120 DEG C, and cooling obtains lubricant oil composite.
Embodiment 3
Step 1, the preparation of modified vegetable oil: by weight, taking 110 parts of soybean oil, adds acid cation exchange 2 parts of resin, be warming up to 55 DEG C, be slowly added dropwise 8 parts of hydrogen peroxide, 5 parts of formic acid reacted, the reaction time be after being added dropwise again into It row 2 hours, after reaction, is washed, separates water layer, the modified soybean oil on upper layer carries out water with 55 DEG C of hot distilled water It washes, discards water phase, then neutralized with alkali, then be washed to pH neutrality with distilled water and be modified after vacuum distillation removes moisture Vegetable oil;
Step 2, by weight, by 35 parts of pentaerythrite, 25 parts of ethanedioic acid, 25 parts of oleanonic acid, 4 parts of catalyst, 110 parts of organic solvent are uniformly mixed, and then heat up, are reacted, the reaction time is 3 hours, 80 DEG C of reaction temperature, is steamed organic Solvent obtains polyol ester;
Step 3, by weight, by 72 parts of modified vegetable oil, 8 parts of polyol ester, four hexyl diphenylamines 0.06 of antioxidant Part, 0.07 part of metal system sulfonate antirust agent, 0.08 part of phosphite ester compound extreme pressure anti-wear additives and succinic acid esters are ashless It is 0.08 part of detergent dispersant to be uniformly mixed, be heated to 100 DEG C, cooling obtains lubricant oil composite.
Reference examples 1
Difference with embodiment 3 is: not being modified to soybean oil.
Step 1, by weight, by 35 parts of pentaerythrite, 25 parts of ethanedioic acid, 25 parts of oleanonic acid, 4 parts of catalyst, 110 parts of organic solvent are uniformly mixed, and then heat up, are reacted, the reaction time is 3 hours, 80 DEG C of reaction temperature, is steamed organic Solvent obtains polyol ester;
Step 2 will pass through 72 parts of pretreated vegetable oil, 8 parts of polyol ester, four hexyl two of antioxidant by weight 0.06 part of aniline, 0.07 part of metal system sulfonate antirust agent, 0.08 part of phosphite ester compound extreme pressure anti-wear additives and succinic acid Esters are ashless 0.08 part of system's detergent dispersant be uniformly mixed, be heated to 100 DEG C, it is cooling, obtain lubricant oil composite.
Reference examples 2
Difference with embodiment 3 is: soybean oil is without pretreatment.
The preparation of modified vegetable oil: step 1 by weight, takes without the pretreated soybean oil 110 of the above method Part, add 2 parts of acid cation exchange resin, be warming up to 55 DEG C, be slowly added dropwise 8 parts of hydrogen peroxide, 5 parts of formic acid reacted, Reaction time is to carry out again after being added dropwise 2 hours, after reaction, is washed, and water layer, the modified soybean oil on upper layer are separated It is washed with 55 DEG C of hot distilled water, discards water phase, then neutralized with alkali, then be washed to pH neutrality, decompression with distilled water After moisture is distilled off, modified vegetable oil is obtained;
Step 2, by weight, by 35 parts of pentaerythrite, 25 parts of ethanedioic acid, 25 parts of oleanonic acid, 4 parts of catalyst, 110 parts of organic solvent are uniformly mixed, and then heat up, are reacted, the reaction time is 3 hours, 80 DEG C of reaction temperature, is steamed organic Solvent obtains polyol ester;
Step 3, by weight, by 72 parts of modified vegetable oil, 8 parts of polyol ester, four hexyl diphenylamines 0.06 of antioxidant Part, 0.07 part of metal system sulfonate antirust agent, 0.08 part of phosphite ester compound extreme pressure anti-wear additives and succinic acid esters are ashless It is 0.08 part of detergent dispersant to be uniformly mixed, be heated to 100 DEG C, cooling obtains lubricant oil composite.
Reference examples 3
Difference with embodiment 3 is: oleanonic acid is not added in step 2, but is all replaced with ethanedioic acid.
Step 1, the preparation of modified vegetable oil: by weight, taking 110 parts of soybean oil, adds acid cation exchange 2 parts of resin, be warming up to 55 DEG C, be slowly added dropwise 8 parts of hydrogen peroxide, 5 parts of formic acid reacted, the reaction time be after being added dropwise again into It row 2 hours, after reaction, is washed, separates water layer, the modified soybean oil on upper layer carries out water with 55 DEG C of hot distilled water It washes, discards water phase, then neutralized with alkali, then be washed to pH neutrality with distilled water and be modified after vacuum distillation removes moisture Vegetable oil;
Step 2 by weight mixes 35 parts of pentaerythrite, 50 parts of ethanedioic acid, 4 parts of catalyst, 110 parts of organic solvent It closes uniformly, then heats up, reacted, the reaction time is 3 hours, 80 DEG C of reaction temperature, steams organic solvent, obtains polyalcohol Ester;
Step 3, by weight, by 72 parts of modified vegetable oil, 8 parts of polyol ester, four hexyl diphenylamines 0.06 of antioxidant Part, 0.07 part of metal system sulfonate antirust agent, 0.08 part of phosphite ester compound extreme pressure anti-wear additives and succinic acid esters are ashless It is 0.08 part of detergent dispersant to be uniformly mixed, be heated to 100 DEG C, cooling obtains lubricant oil composite.
Performance test
1, the wear-resistant test of high temperature
The wear-resistant test of high temperature of oil product is carried out using SRV frictional testing machine, experimental condition is load 300N, frequency 50Hz, stroke 1mm, 120 DEG C of temperature.
2, spot distributed test
Spot distributed test method is 1g program VG engine sludge to be added in 2g test oil, after ultrasonic disperse 6min, Heat 2h in 200 DEG C of baking ovens, then by oil droplet on filter paper, after 24 hours measure oil mark dispersion loop diameter and greasy filth diameter it Than as dispersion index.Dispersion index is higher, and the dispersibility for illustrating oil product is better.
3, QZX experiment
The equipment of use is the 25B-19 type coking plate instrument of Japanese Meitech company production, and the test simulation engine is bent The operating condition of axle box and cylinder liner piston ring lubrication oil circulation makes the process for testing the constantly heated oxidation coking of oil product.When test Between be 6h, oil temperature be 150 DEG C, plate temperature be 320 DEG C.
4, BRT ball rust test
BRT ball rust test is to replace program II D engine rig test, is mainly used to the anti-corruption of engine evaluated oil Erosion and corrosion ability.During entire bench test in 18 hours, test oil guard metal ball continuous contact acidic liquid and Air.Gray scale test is carried out by metal spherical reflector intensity after the end of the test, for determining corroded area, to evaluate examination Test the resistant to rust ability of oil.Acetic acid/hydrobromic acid/hydrochloric acid/deionized water injection rate is 0.19 ml/hour, and air draught is 40 ml/mins, oil temperature are 48 DEG C.
5, biological degradability is the experiment side according to the CEC L-33-A-93(predecessor of the European Community for CEC L-33-T-82) Method.
The result tested above is as shown in the table:
As can be seen from the table, methanol engine lubricating oil provided by the invention has good wear resistance;Especially It is embodiment 3 for reference examples 1, having carried out epoxy-modified improve later to soybean oil can be improved its biodegrade Speed, while can also improve greasy property.Embodiment 3 is for reference examples 2, after being pre-processed to soybean oil, energy Enough improve wear-resisting property.Embodiment 3 joined oleanonic acid in the esterification reaction, be prepared for reference examples 3 Synthetic ester the greasy property of lubricating oil can be made to improve.

Claims (6)

1. a kind of preparation method of the degradable methanol engine lubricating oil of improved plant oil base, which is characterized in that including just like Lower step:
Step 1, the preparation of modified vegetable oil: by weight, taking 100~120 parts of soybean oil, adds acid cation exchange 1~3 part of resin, heating, be slowly added dropwise 5~10 parts of hydrogen peroxide, 3~6 parts of formic acid reacted, after reaction, washed, Separate water layer, the distilled water of the modified soybean oil heat on upper layer is washed, discard water phase, then neutralized with alkali, then with steam Distilled water is washed to pH neutrality and obtains modified vegetable oil after vacuum distillation removes moisture;
Step 2, by weight, by 30~40 parts of polyalcohol, 20~30 parts of ethanedioic acid, 20~30 parts of oleanonic acid, catalysis 3~5 parts of agent, 80~120 parts of organic solvent be uniformly mixed, then heat up, reacted, steam organic solvent, obtain polyalcohol Ester;
Step 3 by 70~80 parts of modified vegetable oil, 5~10 parts of polyol ester, 0.05~1 part of antioxidant, is prevented by weight 0.05~1 part of agent of rust, 0.05~1 part of extreme pressure anti-wear additives and 0.05~1 part of ashless system's detergent dispersant are uniformly mixed, and are heated to 70 It is~120 DEG C, cooling, obtain lubricant oil composite;
In the step 1, soybean oil is needed by pretreatment, and the preprocess method is as follows: taking 200mL soybean oil, adds The ammonium hydroxide of the about 4wt% of oil volume a quarter is added in 20min, continues after adding when temperature rises to 35 DEG C for heat 15min is stirred, stirring is then stopped, being warming up to 95 DEG C, keeps 1h;Reaction mixture is poured into separatory funnel, stratification, It separates and rinses oil reservoir with boiling water after soap stock water;The oil reservoir separated is warming up to 93~97 DEG C again, is added thereto in 10 minutes The H of the 30wt% of oil volume 5%2O2, stop stirring, keep the temperature 1h at 120 DEG C;Stratification separates soap stock water with separatory funnel; Oil reservoir, then stratification are rinsed with boiling water, water layer is removed, obtains pretreated soybean oil.
2. the preparation method of the degradable methanol engine lubricating oil of improved plant oil base according to claim 1, special Sign is: in the step 1, heating is to make temperature to 50~60 DEG C, and the reaction time is that carry out 1~3 after being added dropwise again small When.
3. the preparation method of the degradable methanol engine lubricating oil of improved plant oil base according to claim 1, special Sign is: in the step 1,50~60 DEG C of temperature of the distilled water of the heat.
4. the preparation method of the degradable methanol engine lubricating oil of improved plant oil base according to claim 1, special Sign is: in the step 2, the polyalcohol in hydroxymethyl-propane, glycerine, pentaerythrite, mannitol one Kind or several mixing.
5. the preparation method of the degradable methanol engine lubricating oil of improved plant oil base according to claim 1, special Sign is: the reaction time in the step 2 is 2~4 hours, 70~90 DEG C of reaction temperature.
6. the preparation method of the degradable methanol engine lubricating oil of improved plant oil base according to claim 1, special Sign is: the extreme pressure anti-wear additives are phosphate compounds, phosphite ester compound, sulphur phosphorus complexing agent or sulfur-bearing extreme pressure Agent.
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