CN106699806A - Low-impurity content zinc dialkyl dithiophosphate and preparation method and application thereof - Google Patents
Low-impurity content zinc dialkyl dithiophosphate and preparation method and application thereof Download PDFInfo
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- CN106699806A CN106699806A CN201510783549.7A CN201510783549A CN106699806A CN 106699806 A CN106699806 A CN 106699806A CN 201510783549 A CN201510783549 A CN 201510783549A CN 106699806 A CN106699806 A CN 106699806A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/06—Phosphorus compounds without P—C bonds
- C07F9/16—Esters of thiophosphoric acids or thiophosphorous acids
- C07F9/165—Esters of thiophosphoric acids
- C07F9/17—Esters of thiophosphoric acids with hydroxyalkyl compounds without further substituents on alkyl
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M137/00—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus
- C10M137/02—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing phosphorus having no phosphorus-to-carbon bond
- C10M137/04—Phosphate esters
- C10M137/06—Metal salts
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/045—Metal containing thio derivatives
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/06—Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/25—Internal-combustion engines
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Abstract
The invention discloses low-impurity content zinc dialkyl dithiophosphate (ZDDP). In the zinc dialkyl dithiophosphate, phosphorus is volatile impurity phosphorus and available phosphorus; the molar percentage content of the volatile impurity phosphorus measured through a 31P-NMR spectrum does not exceed 7.2% of the total phosphorus content of the zinc dialkyl dithiophosphate. The invention further provides a preparation method of the low-impurity content zinc dialkyl dithiophosphate. The zinc dialkyl dithiophosphate provided by the invention has low impurity content and high available phosphorus content, has excellent volatility resistance and better oxidation resistance, wear resistance, corrosion resistance and other properties, and can effectively reduce the using mount in engine and transmission lubricating oil and reduce the risk of poisoning failure of an exhaust gas treatment catalyst.
Description
Technical field
The present invention be more particularly directed to a kind of zinc dialkyl dithiophosphate of low impurity content, its preparation method and application, category
In engine and transmission lubricant field.
Background technology
Zinc dialkyl dithiophosphate (ZDDP) as the wear-resistant anti-rotten multifunction additive of antioxygen, in lubricating oil
More than 60 years, be function admirable and most comprehensive multifunction additive, in the prior art still without a kind of additive energy
Replace ZDDP completely.Research in recent years find, the p and ses in zinc dialkyl dithiophosphate can cause Particulate Emission and
Other pollutant emissions increase.Additionally, the easily accumulation of phosphorous volatile matter is in the active metal catalyst position of exhaust catalytic converter
On point, cause catalyst poisoning, cause catalytic efficiency to reduce, exhaust emissions is unqualified.With the hair of GF-4 standards
Cloth, phosphorus content requirement is less than 0.08%, while also requiring to improve oxidation stability, wear resistance etc..In order to meet
Anti-oxidant, wear-resistant and control deposit requirement, it is necessary to more additives are added in formula, or improves addition
The performance of agent single dose.
Known references, such as US4263150, US4289635, US4308154, US4417990, EP0666264,
The disclosure such as US3328335, US3843530, US4957649, production and commercialized ZDDP, the skill of common concern
Art index is the content and zinc-phosphorus ratio of zinc and phosphorus, and its phosphorus content refers to total phosphorus content in ZDDP products, comprising waving
The content of hair property foreign matter of phosphor and available phosphorus.The common structure containing phosphorus impurities includes (RO)2P(S)SR、(RS)3P(S)、
[(RO)2P(S)]2S、(RO)2P(S)H、(RO)3P(S)、(RO)2P(S)OH、[(RO)2P(O)]2S etc.【Lin Yichao, ripple
Spectroscopy magazine, 13 (4) in 1996:365-370】, these are not only mistakened as being available phosphorus content containing phosphorus impurities, also significantly
Reduce the quality of ZDDP.Meanwhile, research shows, the impurity containing P in ZDDP is volatile because without metal,
Easily cause catalyst poisoning.Then, there is no document report to cross at present can effectively control phosphorous impurity content in ZDDP
Method.
The content of the invention
In view of deficiency of the prior art, the dialkyl group two it is a primary object of the present invention to provide a kind of low impurity content
D2EHDTPA zinc, with the impurity content far below commercial product, ZDDP active ingredients high, can reduce its
Consumption in engine and transmission lubricant.
The present invention also aims to provide a kind of side of the zinc dialkyl dithiophosphate for synthesizing the low impurity content
Method, to reduce the impurity content of ZDDP single doses, volatile component particularly therein improves available phosphorus content, together
The performances such as Shi Youhua its antioxygen, wear-resistant and anti-corruption.
Application the present invention also aims to provide the zinc dialkyl dithiophosphate of the low impurity content.
To realize aforementioned invention purpose, the technical solution adopted by the present invention includes:
A kind of zinc dialkyl dithiophosphate of low impurity content, the dialkyl disulfides are provided in certain embodiments
It is volatile impurity phosphorus and available phosphorus for the phosphorus in trbasic zinc phosphate, wherein the mole percent level of the volatile impurity phosphorus
No more than 7.2% of total phosphorus content in the zinc dialkyl dithiophosphate.
Further, in the zinc dialkyl dithiophosphate of the low impurity content, Mole percent of the non-salt containing phosphorus impurities
Than content no more than 7.2%, preferably more than 7.0% of total phosphorus content in the zinc dialkyl dithiophosphate, especially
Preferably shorter than 6.5%.
Further, in the zinc dialkyl dithiophosphate of the low impurity content, zinc dialkyl dithiophosphate
Mass content is 10-99%.
A kind of method of the zinc dialkyl dithiophosphate for synthesizing the low impurity content is provided in certain embodiments,
Including:
Reacted to comprising sulphur phosphoric acid is introduced in diluent, zinc compound, the mixture of organic metal salt, and
The reaction is kept in first temperature range, zinc compound and the first catalyst is added and is formed slurry;
In the range of second temperature, reacted to addition sulphur phosphoric acid in the slurry, and in the second temperature scope
The reaction is kept, the second catalyst is added and is proceeded reaction, reactant mixture is post-treated, obtains described low miscellaneous
The zinc dialkyl dithiophosphate of matter content.
The zinc dialkyl dithiophosphate of any one foregoing low impurity content is provided in certain embodiments or by foregoing
The zinc dialkyl dithiophosphate of low impurity content obtained in any one method is used as the wear-resistant anti-rotten multifunction additive of antioxygen
Purposes.
A kind of compositions of additives, the dioxane comprising any one foregoing low impurity content are provided in certain embodiments
Base zinc dithiophosphate or as obtained in foregoing any one method low impurity content zinc dialkyl dithiophosphate.
Further, the zinc dialkyl dithiophosphate of the low impurity content is effective in the compositions of additives
Addition is 0.001%-5%.
A kind of lubricating composition, the dioxane comprising any one foregoing low impurity content are provided in certain embodiments
Base zinc dithiophosphate or as obtained in foregoing any one method low impurity content zinc dialkyl dithiophosphate.
In certain embodiments there is provided the zinc dialkyl dithiophosphate comprising foregoing low impurity content, by foregoing
Any one in the zinc dialkyl dithiophosphate of low impurity content, foregoing lubricating composition obtained in a kind of method
Device.
Further, described device includes engine or transmission device, but not limited to this.
Compared with prior art, the present invention at least has following good effect:
(1) zinc dialkyl dithiophosphate that the present invention is provided has a low impurity content, available phosphorus content high, together
When also there is excellent anti-volatile, the more preferably performance such as antioxygen, wear-resistant and anti-corruption, and be effectively reduced in engine and
The risk of usage amount and reduction catalyst poisoning in transmission lubricant;
(2) method provided using the present invention can synthesize the zinc dialkyl dithiophosphate of described low impurity.
Specific embodiment
The above quite roughly outlines the features of the present invention and technological merit, to more fully understand subsequent this hair
Bright detailed description.Other feature of the present invention and advantage is described below, they constitute claims of the present invention
Theme.It should be appreciated that disclosed principle and specific embodiment can be easily used as to change or designing reality
Apply the basis of other systems of identical purpose of the invention.It should also be appreciated that such equivalents are without departing from appended
The present invention proposed in claim.With reference to result, it is considered as the present invention to be better understood from following description
Feature assembled about it and operating method novel feature, and other objects and advantages.
One aspect of the present invention provides a kind of zinc dialkyl dithiophosphate of low impurity content, in particular low to wave
Zinc dialkyl dithiophosphate of the hair property containing phosphorus impurities.
More specifically, among the zinc dialkyl dithiophosphate of the low impurity content that the present invention is provided, volatile impurity
The mole percent level of phosphorus particularly, is led to no more than 7.2% of total phosphorus content in the zinc dialkyl dithiophosphate
Cross31The phosphorous impurity content of non-salt that P-NMR spectrums are measured is more preferably small no more than 7.2%, preferably more than 7.0%
In 6.5%.
The zinc dialkyl dithiophosphate of low impurity content of the invention, in particular improving antioxygen, wear-resistant and anti-corruption has
Imitate the zinc dialkyl dithiophosphate of the relative amount of composition.
The non-salt of the ZDDP of low impurity content of the invention has containing phosphorus impurities well below commercially produced product, and ZDDP
Effect composition is high, can reduce its consumption in engine and transmission lubricant.
Another aspect provides a kind of synthesis low zinc dialkyl dithiophosphate method containing phosphorus impurities,
It can include:
Reacted by sulphur phosphoric acid is introduced at least one diluent, zinc compound and organic metal salt mixture,
Under suitable temperature conditionss, such as at 0-100 DEG C, to introducing additional amount of ZnO in batches in above-mentioned reactant mixture,
And add the first catalyst to form slurry at the appropriate time;Then in suitable temperature, such as 50-150 DEG C, upwards
State and add additional amount of sulphur phosphoric acid in slurry, while after the reaction certain hour is kept in the temperature range, then add
Enter the second catalyst to react, the post-treated dialkyl dithio phosphorus for obtaining the low impurity content of reactant mixture
Sour zinc product.
In synthetic method of the invention, at least one organic metal salt is used to suppress impurity generation and closed as zinc impregnation
The auxiliary dispersants of thing, its species may include carboxylic metallic salt, organic phosphate, alkyl-thio-phosphate, dialkyl group
One kind of metal dithiophosphate or its mixture.Zinc compound is comprising in zinc oxide, zinc hydroxide or zinc carbonate
Any one or its mixture, it is preferable to zinc oxide.In preferred embodiment more, the organic gold for using
Category salt can be organic phosphate/alkyl-thio-phosphate/dialkyl dithiophosphate, such as ZDDP.Other one
In a little more preferred embodiments, the organic metal salt for using can selected from organic phosphate, alkyl-thio-phosphate,
The ZDDP of dialkyl dithiophosphate mixing.In other more preferred embodiment, used is organic
Slaine also can be by (instant) the reaction generation in original position.
In synthetic method of the invention, temperature is preferably controlled in 0-100 DEG C when adding zinc compound, especially preferably
40-80 DEG C, more preferably 42-65 DEG C, impurity generation can be reduced and prevent from generating the aggregate of zinc compound.
It is to add the second catalyst, second catalysis in suitable temperature and time in synthetic method of the invention
Agent may be selected from but be not limited to water, metal salt of organic carboxylic acid, organic carboxyl acid ammonium salt a kind of or its mixture, for example, can be excellent
Selected from salts of carboxylic acids, acetic acid ammonium salt and its mixture or the aqueous solution, more preferably from zinc acetate and zinc acetate aqueous solution.
In some embodiments of the invention, the aqueous solution of zinc acetate can be added, the wherein consumption of zinc acetate about zinc total moles are used
The 0.1-50% of amount.Wherein, the addition of the second catalyst, the generation and/or decomposition that can substantially reduce impurity has been generated
Impurity.
It is that reactant mixture is post-processed in suitable temperature in synthetic method of the invention, temperature can be with excellent
Elect 50-120 DEG C, especially preferably 80-95 DEG C, the impurity that generation can be avoided unnecessary as.
In some embodiments of the present invention, synthesized ZDDP is used as lubricant oil concentrate and lubricating oil
Additive.These lubricant oil concentrates and lubricating oil can be added in engine and transmission device.
In of the invention one more specific case study on implementation, aforementioned synthetic methods may include steps of:
Reacted by sulphur phosphoric acid is introduced in diluent, zinc compound and organic metal salt mixture;
The reaction is kept in the first temperature range, while to above-mentioned mixed comprising diluent, zinc compound and slaine
Other quantity zinc compound and catalyst are introduced in compound to form slurry;
In second temperature scope, to additional amount of sulphur phosphoric acid is added in above-mentioned slurry, while in the temperature range
Keep the reaction;
The second catalyst is added to form zinc dialkyl dithiophosphate in the second temperature scope.
Post processing above reactant obtains zinc dialkyl dithiophosphate product.
In synthetic method of the invention, foregoing diluent may be selected from but be not limited to base oil, alkane, aromatic hydrocarbons, halo
One kind in hydrocarbon, alcohol, ether, ketones solvent or both and more than.Wherein base oil can be natural oil, artificial oil
Or their mixture.
Wherein, natural oil may be selected from but be not limited to animal oil and vegetable oil (such as castor oil, lard), liquid petroleum and
The mineral oil of alkane, the hydrofinishing of cycloalkanes and mixing alkane-naphthene types, solvent treatment or acid treatment, from coal
The oil of the lubricant viscosity of charcoal or shale also serves as useful base oil.
Wherein, artificial oil may be selected from but be not limited to hydrocarbon ils and the hydrocarbon ils of halogen substitution, such as polymerization and the mutually alkene (example of polymerization
Such as, polybutene, polypropylene, propylene-isobutylene copolymers, chlorinated polybutylenes, poly- (1- hexenes), poly- (1- octenes),
Poly- (1- decene));Alkylbenzene is (for example, detergent alkylate, Tetradecylbenzene, dinonyl benzene, two (2- ethyl hexyls
Base) benzene);Polyphenyl (for example, biphenyl, terphenyl, polyphenol of alkylation);Diphenyl ether and alkylation with alkylation
Diphenyl sulfide and its derivative, analog and homologue.Gas from Fiscber-Tropscb synthesis hydrocarbon to liquid technique artificial oil also
It is useful, they are commonly referred to gas to liquid, or " GTL " base oils.
Wherein oneself warp of terminal hydroxyl passes through the modified oxyalkylene polymer such as esterification, etherificate and interpretation and their derivative
Thing constitutes another kind of known artificial oil.Their example includes being prepared by the polymerization of ethylene oxide or propylene oxide
Polyoxyalkylene polymers, and polyoxyalkylene polymers alkyl and aryl ether (for example, molecular weight be 1000 methyl-
Poly- Isopropanediol ether or molecular weight are the diphenyl ether of the polyethylene glycol of 1000-1500);With their list and polybasic carboxylic acid
Ester, such as acetic acid esters, the oxygen-containing acid diesters of the C13 of C3-C8 fatty acid esters and TEG of mixing.
Another kind of suitable synthetic lubricant fluid includes dicarboxylic acids (such as phthalic acid, butanedioic acid, alkyl succinic acid
With alkenyl succinic acid, maleic acid, azelaic acid, suberic acid, decanedioic acid, fumaric acid, adipic acid, linoleic acid dimer,
Malonic acid, alkyl malonic acid, alkenyl malonic etc.) with various alcohol (such as butanol, hexanol, lauryl alcohol, 2- ethyls
Hexanol, ethylene glycol, diethylene glycol monoether, propane diols etc.) ester.
Can be used as the ester of artificial oil also include by C5-C12 monocarboxylic acids and polyalcohol and polyol ester such as neopentyl glycol,
Trimethylolpropane, pentaerythrite, dipentaerythritol, tripentaerythritol be made those.
Oil based on silicon such as poly- alkyl, poly- aryl, poly-alkoxyl or poly- aryloxy group silicone oil and silicic acid ester oil constitute another
The useful syntholube of class;This oil includes tetraethyl orthosilicate, the isopropyl ester of silicic acid four, silicic acid four (2- ethylhexyls)
Ester, silicic acid four (4- methyl -2- ethylhexyls) ester, silicic acid four (to tert-butyl-phenyl) ester, six (4- methyl -2- second
Base hexyl) disiloxane, poly- (methyl) siloxanes and poly- (aminomethyl phenyl) siloxanes.Other synthetic lubricant fluid bags
Include phosphorous sour liquid ester (such as diethyl ester of tricresyl phosphate, trioctyl phosphate, decylphosphonic acid) and poly-
Tetrahydrofuran.
In synthetic method of the invention, foregoing organic metal salt can be carboxylic metallic salt, organic phosphate, alkyl
Thiophosphate, one kind of dialkyl dithiophosphoric acid slaine or its mixture, the carboxylic acid group include C1-C18
The hydroxy-acid group of alkyl, aryl and halogen, sulphur, phosphorus heteroatoms substituted hydrocarbon radical etc.;The dialkyl dithiophosphoric acid base
Any commercialized sulphur phosphoric acid and its mixture are may be selected from, is generated also selected from by any C3-C18 alcohol, alkyl phenol
Single or mix sulphur phosphoric acid;The metal is including sodium, potassium, magnesium, calcium, barium, iron, cobalt, nickel, copper, zinc etc..
Foregoing sulphur phosphoric acid may be selected from any commercialized sulphur phosphoric acid and its mixture, also selected from by any alkyl, cycloalkanes
It is single or mixed that the alcohol and phosphorus pentasulfide of base, aralkyl or alkaryl and the basic alkyl with similar structures are generated
Close sulphur phosphoric acid;The alcohol includes straight chain and side chain and the primary, secondary, tertiary and quaternary alcohol and its mixture of isomerization.It is so-called
Basic hydrocarbon refers to the base containing substitution, and such as ether, ester group, nitro and halogen, these groups do not influence this alkyl substantially
That hydrocarbon of hydrocarbon characteristic.
Described alkyl may be selected from but be not limited to isopropyl, isobutyl group, normal-butyl, sec-butyl, various amyl groups, heptyl,
2- ethylhexyls, double isobutyl groups, iso-octyl, nonyl, docosyl, decyl, dodecyl, three decyls etc..Institute
The alkane phenyl for enumerating is etc. butylbenzene base, penta phenyl, dodecylphenyl, heptan phenyl.Cycloalkyl is also similarly have
, and they mainly include cyclohexyl and relatively low alkyl-cyclohexyl group.Most substituted hydrocarbon radicals can also be used,
Such as chloro amyl group, dichloro- phenyl and dichloro- decyl.
The preparation method of foregoing sulphur phosphoric acid can be all known commercialized production methods, or
The synthetic method being widely known by the people in the patents such as US4263150, US4289635, US4308154, US4417990.
Above-mentioned patent is incorporated into present specification by being cited these disclosures herein.I.e. by phosphorus pentasulfide with
The mixture phase reaction of a kind of alcohol, a kind of phenol, the mixture of alcohol or alcohol and phenol prepares this sulphur phosphoric acid.Every mole five vulcanization
Alcohol of two phosphorus with 4-5 moles or phenol participate in reaction, and the temperature of this reaction can be in about 50 DEG C~about 200 DEG C of scope
Inside carry out.
Foregoing first catalyst includes acid, ammonium carboxylate salt and carboxylic metallic salt;Sour preferred aliphatic series acid or alicyclic carboxylic acid,
Can be monocarboxylic acid and polybasic carboxylic acid, generally contain from 1 to about 3 carboxyl, preferably containing only 1 carboxyl.Carboxylic acid can
With containing from about 2 to about 40 carbon atoms, preferably containing from about 2 to about 20 carbon atoms, preferably containing about 2 to about
8 carbon atoms.Preferred carboxylic acid is the carboxylic acid with general formula R COOH, and R is aliphatic series or cycloaliphatic hydroxyl group in formula.
Suitable acid includes ethanol, propionic acid, butyric acid, valeric acid, caproic acid, octanoic acid, n-nonanoic acid, capric acid, lauric acid/dodecanoic acid, stearic acid
With 20 acid, and olefinic acid, such as oleic acid, linoleic acid, linolenic and linoleic dimer.Preferred polynary carboxylic
Acid can be butanedioic acid, alkane tomb and alkenyl succinic, hexanedioic acid, decanedioic acid and citric acid etc..The ammonium carboxylate salt
And carboxylic metallic salt, including aforementioned carboxylic acid ammonium salt and carboxylic metallic salt.The preferred acetic acid of catalyst, ammonium acetate and
Zinc acetate.
Foregoing first temperature range at 0-100 DEG C, preferably 40-80 DEG C, more preferably 42-65 DEG C.
Foregoing second temperature scope at 50-150 DEG C, preferably 60-125 DEG C, more preferably 70-90 DEG C.
Foregoing second catalyst may be selected from water, carboxylic metallic salt, ammonium carboxylate salt one kind or its mixture.Carboxylic metallic salt,
Carboxylic acid in ammonium carboxylate salt may be selected from aliphatic acid or alicyclic carboxylic acid, can be monocarboxylic acid and polybasic carboxylic acid, generally contain
From 1 to about 3 carboxyl, preferably containing only 1 carboxyl.Carboxylic acid can contain from about 2 to about 40 carbon atoms, preferably contain
From about 2 to about 20 carbon atoms, preferably containing about 2 to about 8 carbon atoms.Preferred carboxylic acid is with formula
The carboxylic acid of RCOOH, R is aliphatic series or cycloaliphatic hydroxyl group in formula.Suitable acid includes ethanol, propionic acid, butyric acid, penta
Acid, caproic acid, octanoic acid, n-nonanoic acid, capric acid, lauric acid/dodecanoic acid, stearic acid and 20 acid, and olefinic acid, such as oleic acid,
Linoleic acid, linolenic and linoleic dimer.Preferred polybasic carboxylic acid can be butanedioic acid, alkane tomb and alkenyl amber
Acid, hexanedioic acid, decanedioic acid and citric acid etc..Wherein preferred scheme is salts of carboxylic acids and acetic acid ammonium salt and its mixture
Or the aqueous solution, preferred scheme is zinc acetate and zinc acetate aqueous solution.The water of the preferred zinc acetate of the catalyst of the above second
Solution, zinc acetate consumption is the 0.1-50% molar concentrations of the total consumption of zinc.
Foregoing post-processing approach can have various, for example:
Post-processing approach optionally vacuum can strip the reactant mixture, and temperature is 50-120 DEG C, preferably 80-95 DEG C;
Post-processing approach optionally can filter the reactant mixture to remove solid particle;
Post-processing approach can dilute the reactant mixture optionally with base oil, thus produce the low impurity content
Zinc dialkyl dithiophosphate.
ZDDP of the invention or its mixture can be applied in the formula of lubricating oil, lubricating grease, the ZDDP compounds
With low impurity content, available phosphorus content high, except with wear-resistant, antioxygen and anti-corrosion property, also resists with excellent
Volatility etc..
Technical scheme is described in more detail below by way of some embodiments, but the embodiment is not constituted
Limitation of the present invention.
Explanation:All percentage compositions are molar content below, are bases31P-NMR is calculated.
Embodiment 1 and embodiment 2 (comparative example)
Two classes obtained by commercially available approach mix the commercialization sample ZDDP1 that secondary alkyl ZDDP, multiple commercial vendors are produced
And ZDDP2, any change is not added with, directly test.Test to obtain impurity phosphorus content average out to 7.38% and 7.65%, alkali
Formula ZDDP contents average out to 23% and 27%.
Embodiment 3
The present embodiment refers to EP0866113 using the homemade secondary alkyl sulfide phosphoric acid of mixing, its preparation method, its alcohol knot
Structure and ratio are identical with embodiment 1 and embodiment 2.
By 10g base oils (150N), 0.5gZnO and 5g mix secondary alkyl sulfide phosphoric acid be added to be equipped with puddler,
In four neck round-bottom flasks of thermometer, condenser pipe and dropping funel, in dispersed with stirring at 45 DEG C.Then keep temperature
At 40-60 DEG C, 7.0g ZnO are dividedly in some parts, add 0.07g glacial acetic acid.75 DEG C are warmed up to, 45g sulphur phosphoric acid is added dropwise.
Completion of dropwise addition, after reaction 2h, adds the 3g saturated acetic acid zinc aqueous solution.After reacting 2h again, 95 DEG C are warming up to, subtracted
Pressure distillation 30min, the impurity such as water removal and alcohol.Subsequent diatomite drainage, removes solid impurity, obtains ZDDP products.
Test foreign matter of phosphor be 4.1%, alkali formula ZDDP contents be 24%.
Embodiment 4
The present embodiment refers to EP0866113 using the homemade secondary alkyl sulfide phosphoric acid of mixing, preparation method, average each alcohol
Containing about 4.5 carbon atoms, its alcohol structure and ratio are identical with sulphur phosphoric acid used in embodiment 1.
By 10g base oils (150N), 0.5g ZnO and 5g mix secondary alkyl sulfide phosphoric acid be added to be equipped with puddler,
In four neck round-bottom flasks of thermometer, condenser pipe and dropping funel, in dispersed with stirring at 45 DEG C.Then keep temperature
At 40-60 DEG C, 6.35g ZnO are dividedly in some parts, add 0.07g glacial acetic acid.75 degree are warmed up to, 45g sulphur phosphoric acid is added dropwise.
Completion of dropwise addition, after isothermal reaction 4h, is warming up to 95 DEG C, vacuum distillation 30min, the impurity such as water removal and alcohol.Subsequent silicon
Diatomaceous earth drainage, removes solid impurity, obtains ZDDP products.Test foreign matter of phosphor be 6.2%, alkali formula ZDDP contents
2%.
Embodiment 5
The present embodiment contains about 4.5 carbon atoms, preparation side using the homemade secondary alkyl sulfide phosphoric acid of mixing, average each alcohol
Method refers to EP0866113, and its alcohol structure and ratio are identical with sulphur phosphoric acid used in embodiment 1.
By 10g base oils (150N), 0.5gZnO and 5g mix secondary alkyl sulfide phosphoric acid be added to be equipped with puddler,
In four neck round-bottom flasks of thermometer, condenser pipe and dropping funel, in dispersed with stirring at 45 DEG C.Then keep temperature
At 40-60 DEG C, 6.35gZnO is dividedly in some parts, adds 0.07g glacial acetic acid.75 DEG C are warmed up to, 45g sulphur phosphoric acid is added dropwise.
Completion of dropwise addition, after reaction 2h, adds the 3g saturated acetic acid zinc aqueous solution.After reacting 2h again, 95 DEG C are warming up to, subtracted
Pressure distillation 30min, the impurity such as water removal and alcohol.Subsequent diatomite drainage, removes solid impurity, obtains ZDDP products.
Test foreign matter of phosphor be 5.9%, alkali formula ZDDP contents 13.4%.
Embodiment 6 (comparative example)
The present embodiment uses homemade pair of Xin Baiji sulphur phosphoric acid, its preparation method to refer to EP0866113.
21g base oils (150N), 0.5gZnO and 25g sulphur phosphoric acid are added to and are equipped with puddler, thermometer, cold
In four neck round-bottom flasks of solidifying pipe and dropping funel, in dispersed with stirring at 55 DEG C.40-60 DEG C then is kept the temperature at,
7.51g ZnO are dividedly in some parts, 0.07g glacial acetic acid is added.75 DEG C are warmed up to, 45g sulphur phosphoric acid is added dropwise.Completion of dropwise addition,
After reaction 4h, 95 DEG C, vacuum distillation 30min, the impurity such as water removal and alcohol are warming up to.Subsequent diatomite drainage, removes
Solid impurity, obtains ZDDP products.Test foreign matter of phosphor be 6.4%, alkali formula ZDDP contents be 16.5%.
Embodiment 7
The present embodiment uses homemade pair of Xin Baiji sulphur phosphoric acid identical with embodiment 6.
21g base oils (150N), 0.5gZnO and 25g sulphur phosphoric acid are added to and are equipped with puddler, thermometer, cold
In four neck round-bottom flasks of solidifying pipe and dropping funel, in dispersed with stirring at 55 DEG C.40-60 DEG C then is kept the temperature at,
7.51g ZnO are dividedly in some parts, 0.07g glacial acetic acid is added.75 DEG C are warmed up to, 45g sulphur phosphoric acid is added dropwise.Completion of dropwise addition,
After reaction 2h, 1.36g deionized waters are added.After reacting 2h again, 95 DEG C are warming up to, vacuum distillation 30min is removed
The impurity such as water and alcohol.Subsequent diatomite drainage, removes solid impurity, obtains ZDDP products.Test foreign matter of phosphor be 5.1%,
Alkali formula ZDDP contents are 36.3%.
Embodiment 8 (comparative example)
The present embodiment refers to EP0866113 using homemade mixing primary alkyl sulphur phosphoric acid, its preparation method.
21g base oils (150N), 0.5gZnO and 23g sulphur phosphoric acid are added to and are equipped with puddler, thermometer, cold
In four neck round-bottom flasks of solidifying pipe and dropping funel, in dispersed with stirring at 55 DEG C.40-60 DEG C then is kept the temperature at,
6.93g ZnO are dividedly in some parts, 0.08g glacial acetic acid is added.75 DEG C are warmed up to, 47g sulphur phosphoric acid is added dropwise.Completion of dropwise addition,
After reaction 4h, 95 DEG C, vacuum distillation 30min, the impurity such as water removal and alcohol are warming up to.Subsequent diatomite drainage, removes
Solid impurity, obtains ZDDP products.Test foreign matter of phosphor be 8.1%, alkali formula ZDDP contents be 25.5%.
Embodiment 9
The present embodiment homemade mixes primary alkyl sulphur phosphoric acid using identical with embodiment 8.
21g base oils (150N), 0.5gZnO and 23g sulphur phosphoric acid are added to and are equipped with puddler, thermometer, cold
In four neck round-bottom flasks of solidifying pipe and dropping funel, in dispersed with stirring at 55 DEG C.40-60 DEG C then is kept the temperature at,
7.8g ZnO are dividedly in some parts, 0.12g glacial acetic acid is added.75 DEG C are warmed up to, 47g sulphur phosphoric acid is added dropwise.Completion of dropwise addition,
After reaction 2h, the 2.6g saturated acetic acid zinc aqueous solution is added.After reacting 2h at 80 DEG C again, 95 DEG C, decompression are warming up to
Distillation 30min, the impurity such as water removal and alcohol.Subsequent diatomite drainage, removes solid impurity, obtains ZDDP products.Survey
Try foreign matter of phosphor be 6.7%, alkali formula ZDDP contents be 39.3%.
Embodiment 10-18
As seen from the above embodiment, the ZDDP impurity contents synthesized by the method for the present invention are much smaller than commercial product, greatly
The big quality that improve ZDDP.
Embodiment described above has been described in detail to technical scheme, it should be understood that the above is only
Be specific embodiment of the invention, be not intended to limit the invention, it is all done in spirit of the invention it is any
Modification, supplement or similar fashion replacement etc., should be included within the scope of the present invention.
Claims (10)
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