CN103254966B - Complex-calcium-based tetrapolyurea lubricating grease and preparation method thereof - Google Patents

Complex-calcium-based tetrapolyurea lubricating grease and preparation method thereof Download PDF

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CN103254966B
CN103254966B CN201210041383.8A CN201210041383A CN103254966B CN 103254966 B CN103254966 B CN 103254966B CN 201210041383 A CN201210041383 A CN 201210041383A CN 103254966 B CN103254966 B CN 103254966B
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acid
calcium
lubricating grease
fatty acid
lubricating
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CN103254966A (en
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王佳
孙洪伟
何懿峰
刘磊
翟浩川
段庆华
刘中其
姜靓
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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 relates to a complex-calcium-based tetrapolyurea lubricating grease and a preparation method thereof. The lubricating grease comprises lubricating base oil, tetrapolyurea, and composite calcium soap. The composite calcium soap is a mixture of higher fatty acid calcium, binary aromatic acid calcium, and C1-C6 fatty acid calcium. The invention also relates to a preparation method of the complex-calcium-based tetrapolyurea lubricating grease. The preparation method comprises the steps that: (1) under the existence of a lubricating base oil, diisocyanate, diamine and monoamine are subjected to a contact reaction; and the mixture obtained after the reaction is heated and refined; wherein a dose molar ratio of diisocyanate to diamine to monoamine is (1.9-2.1):1:(1.9-2.1); (2) under the existence of the lubricating base oil, calcium hydroxide, higher fatty acid, binary aromatic acid, and C1-C6 fatty acid calcium are subjected to a contact reaction; and the mixture obtained from the reaction is heated and dehydrated; and (3) the product obtained in the step (1) and the product obtained in the step (2) are mixed. The complex-calcium-based tetrapolyurea lubricating grease provided by the invention has excellent comprehensive performance.

Description

A kind of composite calcium-base four polyurea grease and preparation method thereof
Technical field
The present invention relates to a kind of composite calcium-base four polyurea grease, and this preparation of greases method.
Background technology
Polyurea grease (abbreviation polyurea grease) is the lubricating grease prepared by the organic compound multiviscosisty base oil containing urea groups in molecule.Because polyurea thickening agent is different from metal soap base viscosifying agent, not metal ion, to avoid in soap base viscosifying agent metal ion to the catalysed oxidn of grease base oil, therefore polyurea grease has good oxidation stability and thermostability, makes polyurea grease be more suitable for the lubrication of hot conditions.
At present, the report of article and patent mainly concentrates on preparation and the synthesis aspect of two polyurea greases, and two polyurea grease shear stabilities are poor, works 100,000 times and work 60 cone penetration differences all more than 80 units.Little to the report of four polyurea greases.The salient features such as dropping point, extreme pressure property, colloid stability, oxidation stability of four polyurea greases increases than existing two polyurea greases.Therefore there is more excellent PERFORMANCE OF GREASES, and can be widely used.But, because the shear stability of four polyurea greases is not good, thus limit its application under the working condition of high temperature, high speed and heavy loading.
Complex calcium lubricating grease is the high dropping point grease developed the earliest, a kind of heatproof, withstand voltage, broad-spectrum excellent lubricating grease, there is good mechanical stability, colloid stability and anti-water drenching energy, but sclerosis problem is its widely used lethal factor of restriction, improve the main contents that sclerosis problem is complex calcium lubricating grease research always.
In order to solve the sclerosis problem that complex calcium lubricating grease exists, those skilled in the art attempt to introduce polyurea grease in complex calcium lubricating grease, such as, CN1364859A and CN1657599A individually discloses the calcium base polyurea grease obtained by introducing two polyureas in complex calcium lubricating grease, but the over-all properties of these calcium base polyurea greases is not good.
Summary of the invention
The object of the invention is the above-mentioned defect existed to overcome existing lubricating grease, a kind of new composite calcium-base four polyurea grease and preparation method thereof is provided.
The invention provides a kind of composite calcium-base four polyurea grease, wherein, this lubricating grease contains lubricating base oil, four polyureas and calcium complex soap, and described calcium complex soap is the mixture of the fatty acid calcium of higher fatty acid calcium, binary aromatic acid calcium and C1-C6.
Present invention also offers a kind of preparation method of composite calcium-base four polyurea grease, the method comprises the following steps:
(1) under the existence of lubricating base oil, by vulcabond, diamines and monoamine contact reacts, heat up the mixture obtained after reaction refining, and wherein, the mol ratio of vulcabond, diamines and monoamine is (1.9-2.1): 1: (1.9-2.1);
(2) under the existence of lubricating base oil, by the lipid acid contact reacts of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6, the mixture obtained is carried out intensifications dewater after reaction;
(3) the product mixing that product step (1) obtained and step (2) obtain.
Composite calcium-base four polyurea grease according to the present invention has excellent over-all properties.Concrete, in described composite calcium-base four polyurea grease of the present invention, by introducing four polyureas, overcome the problem of the sclerosis that traditional complex calcium lubricating grease exists; By introducing the mixture of the fatty acid calcium of higher fatty acid calcium, binary aromatic acid calcium and C1-C6, overcome the defect that the over-all properties of traditional polyurea grease existence is bad.
And, compare as the composite calcium-base polyurea grease of composite calcium-base viscosifying agent with the mixture of unitary aromatic acid calcium with by introducing higher fatty acid calcium, described composite calcium-base polyurea grease of the present invention has obviously preferably over-all properties, particularly has preferably mechanical stability, colloid stability and anti-water drenching energy.
Other features and advantages of the present invention are described in detail in embodiment part subsequently.
Accompanying drawing explanation
Fig. 1 is the infrared analysis spectrogram of four polyureas in the lubricating grease of embodiment 1 preparation;
Fig. 2 is the nuclear magnetic resonance spectroscopy spectrogram of four polyureas in the lubricating grease of embodiment 1 preparation;
Fig. 3 is the Electrospray Ionization Mass Spectrometry spectrogram of four polyureas in the lubricating grease of embodiment 1 preparation.
Embodiment
The invention provides a kind of composite calcium-base four polyurea grease, this lubricating grease contains lubricating base oil, four polyureas and calcium complex soap, and described calcium complex soap is the mixture of the fatty acid calcium of higher fatty acid calcium, binary aromatic acid calcium and C1-C6.
Main improvements of the present invention are, the mixture of the fatty acid calcium of higher fatty acid calcium, binary aromatic acid calcium and C1-C6 is used to replace conventional calcium complex soap, as the composite calcium-base viscosifying agent of lubricating grease, to overcome the not good defect of over-all properties that conventional lubricating grease exists, and the respective kind of described lubricating base oil, described four polyureas and described calcium complex soap and content range all can be same or similar with the composite calcium-base polyurea grease of routine.
Under preferable case, relative to the described lubricating base oil of 100 weight parts, the content of described four polyureas is 0.5-22 weight part, is more preferably 3-15 weight part; The content of described calcium complex soap is 2.2-36 weight part, is more preferably 5-25 weight part.
In described calcium complex soap, the ratio of the fatty acid calcium of described higher fatty acid calcium, described binary aromatic acid calcium and described C1-C6 can change in very wide scope.Under preferable case, in order to improve the over-all properties of described lubricating grease further, the ratio of the integral molar quantity of the fatty acid calcium of described higher fatty acid calcium and described binary aromatic acid calcium and described C1-C6 is 1: 0.1-10, is more preferably 1: 0.2-5; And the mol ratio of the fatty acid calcium of described binary aromatic acid calcium and described C1-C6 is 1: 0.1-2, is more preferably 1: 0.2-0.8.
Described calcium complex soap can obtain according to the method for routine, such as, described calcium complex soap can be prepared by being reacted by the lipid acid of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6, and also namely described calcium complex soap can be the saponification reaction product of the lipid acid of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6.Preferably, the ratio of the integral molar quantity of the lipid acid of described higher fatty acid and described binary aromatic acid and described C1-C6 is 1: 0.1-10, is more preferably 1: 0.2-5; And the mol ratio of the lipid acid of described binary aromatic acid and described C1-C6 is 1: 0.1-2, is more preferably 1: 0.2-0.8.More preferably, the ratio of the integral molar quantity of the carboxyl in the lipid acid of the molar weight of calcium hydroxide and the carboxyl in the carboxyl in described higher fatty acid, described binary aromatic acid and described C1-C6 is 0.4-0.6: 1, is more preferably 0.5-0.55: 1.
Described higher fatty acid can be the higher fatty acid that this area routine uses, such as, can be the straight chain fatty acid of C12-C24 or the hydroxy fatty acid of C12-C24.Preferably, described higher fatty acid is be selected from least one in lauric acid, oleic acid, palmitinic acid, stearic acid, 12-oxystearic acid and eicosyl carboxylic acid.
The structural formula of described binary aromatic acid preferably such as formula shown in (I),
Formula (I)
Wherein, R 2, R 3, R 4, R 5and R 6in one be carboxyl, the alkyl of C1-C5 of carboxyl substituted or the aryl of the C6-C12 of carboxyl substituted, R 2, R 3, R 4, R 5and R 6in other four be the fluorinated aryl of hydrogen, the alkyl of C1-C5, the thiazolinyl of C2-C5, the alkynyl of C2-C5, the aryl of C6-C12, the fluoro-alkyl of C1-C5 or C6-C12 independently of one another.
Under preferable case, R 2, R 3, R 4, R 5and R 6in one be the phenyl of carboxyl, carboxymethyl or carboxyl substituted, R 2, R 3, R 4, R 5and R 6in other four be the alkyl of hydrogen or C1-C2 independently of one another.
Still more preferably, described binary aromatic acid is at least one in phthalic acid, m-phthalic acid, terephthalic acid and biphenyl dicarboxylic acid (as 4,4 '-biphenyl dicarboxylic acid).
Most preferably, described binary aromatic acid is terephthalic acid and/or 4,4 '-biphenyl dicarboxylic acid.
The lipid acid of described C1-C6 can be formic acid, acetic acid, propionic acid, butyric acid, valeric acid, caproic acid, oxalic acid, propanedioic acid, succinic acid etc.Under preferable case, the lipid acid of described C1-C6 is be selected from least one in acetic acid, propionic acid, butyric acid and oxalic acid.
Described four polyureas can various four polyureas that use of this area routine, such as can for such as formula the compound shown in (II),
Formula (II)
Wherein, each R 1independently selected from alkyl, cycloalkyl or aryl, R 2be selected from alkylidene group or arylidene, each R 3independently selected from alkylidene group, cycloalkylidene or arylidene.
More preferably, in formula (II), each R 1independently selected from the alkyl of C8-C24, the cycloalkyl of C8-C24 or C6-C10 aryl, R 2be selected from the alkylidene group of C2-C12 or the arylidene of C6-C14, each R 3independently selected from the arylidene of the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or C6-C30.In the present invention, the alkyl of described C8-C24 can be substituted or unsubstituted alkyl, and substituting group can be halogen, such as Cl, Br usually; The cycloalkyl of described C8-C24 can be substituted or unsubstituted cycloalkyl, and substituting group can be halogen, such as Cl, Br usually; Described C6-C10 aryl can be substituted or unsubstituted aryl, and substituting group can be the alkyl of halogen (such as Cl, Br), C1-C5 usually.
Further preferably, in formula (II), each R 1the phenyl that the phenyl replaced independently selected from the alkyl of the cycloalkyl of the alkyl of C10-C18, C10-C18, phenyl, C1-C3 or halogen (such as Cl, Br) replace, R 2be selected from the alkylidene group of C2-C8, phenylene or biphenylene, each R 3independently selected from xylylene or hexylidene between xylene, methylenediphenyl, sub-dicyclohexylmethyl, Asia.
Still more preferably, in formula (II), each R 1independently selected from dodecyl, tetradecyl, hexadecyl, octadecyl, phenyl, tolyl or chlorophenyl, R 2be selected from ethylidene, propylidene, butylidene, pentylidene, hexylidene, phenylene or biphenylene, each R 3independently selected from xylylene or hexylidene between xylene, methylenediphenyl, sub-dicyclohexylmethyl, Asia.
Described lubricating base oil can be the various lubricating base oils that this area routine uses, such as, can be 100 DEG C of viscosity be 2-150mm 2/ s (is preferably 2-100mm 2/ s, is more preferably 8-50mm 2/ s) lubricating base oil.Concrete, described lubricating base oil can be such as at least one in mineral oil, vegetables oil and synthetic oil.Described synthetic oil can be poly-a-olefin oil (PAO), Esters oil, alkyl-silicone oil, F-T synthesis wet goods.
Other various additives that composite calcium-base four polyurea grease according to the present invention can also use containing this area routine, described additive can be such as at least one in extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent.Relative to the described lubricating base oil of 100 weight parts, described additive level can be 0.1-15 weight part, is preferably 0.5-10 weight part.
Described extreme pressure anti-wear additives can be such as at least one in dithio Acidic phosphates zinc, dithio dialkyl amido zinc formate, triphenylphosphorothionate, organic molybdenum complex compound, olefine sulfide, molybdenumdisulphide, tetrafluoroethylene, thiophosphoric acid molybdenum, clorafin, dibutyl dithiocaarbamate antimony, tungsten disulfide, Selenium Sulfide, fluorographite, calcium carbonate and zinc oxide.
Described oxidation inhibitor is preferably arylamine kind antioxidant, and described arylamine kind antioxidant can be such as at least one in the amino p-cresol of pentanoic, di-iso-octyldiphenylamine, phenyl-a-naphthylamine, 2,6 ditertiary butyl p cresol and 2,6-di-t-butyl-alpha, alpha-dimethyl.
Described rust-preventive agent can be such as at least one in barium mahogany sulfonate, petroleum sodium sulfonate, benzothiazole, benzotriazole, zinc naphthenate and alkenyl succinic acid.
Present invention also offers a kind of preparation method of composite calcium-base four polyurea grease, the method comprises the following steps:
(1) under the existence of lubricating base oil, by vulcabond, diamines and monoamine contact reacts, heat up the mixture obtained after reaction refining, and wherein, the mol ratio of vulcabond, diamines and monoamine is (1.9-2.1): 1: (1.9-2.1);
(2) under the existence of lubricating base oil, by the lipid acid contact reacts of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6, the mixture obtained is carried out intensifications dewater after reaction;
(3) the product mixing that product step (1) obtained and step (2) obtain.
Method according to the present invention, implement in the reactor that step (1) is different with step (2) each leisure, by preparing four polyurea greases and complex calcium lubricating grease respectively, then both four polyurea greases and complex calcium lubricating grease are mixed, heat remaining in the preparation process of four polyureas can not be had an impact to the preparation process of calcium complex soap, thus avoid in the preparation process of conventional composite calcium-base polyurea grease the problem easily causing the strong volatilization of small molecules acid.
Step (1) can the preparation method of four polyurea greases conveniently be implemented.
In step (1), there is no particular limitation for the catalytic condition of vulcabond, diamines and monoamine, and such as, described catalytic condition can comprise: temperature of reaction is 60-120 DEG C, and the reaction times is 5-60 minute.
In step (1), the condition of described refining can comprise: temperature is 200-220 DEG C, and the time is 1-30 minute.
Under preferable case, the mol ratio of the consumption of vulcabond, diamines and monoamine is 2: 1: 2.
The general formula of described monoamine can be R 1nH 2, wherein, R 1can be the alkyl of C8-C24, the cycloalkyl of C8-C24 or C6-C10 aryl.The alkyl of described C8-C24 can be substituted or unsubstituted alkyl, and substituting group can be halogen, such as Cl, Br usually; The cycloalkyl of described C8-C24 can be substituted or unsubstituted cycloalkyl, and substituting group can be halogen, such as Cl, Br usually; Described C6-C10 aryl can be substituted or unsubstituted aryl, and substituting group can be the alkyl of halogen (such as Cl, Br), C1-C5 usually.Under preferable case, R 1the phenyl that the phenyl replaced for the alkyl of the cycloalkyl of the alkyl of C10-C18, C10-C18, phenyl, C1-C3 or halogen (such as Cl, Br) replace.Preferred, described monoamine is at least one in aniline, m-chloro aniline, p-Chlorobenzoic acid amide, para-totuidine, amino dodecane, tetradecy lamine, cetylamine and stearylamine.
The general formula of described diamines can be NH 2-R 2-NH 2, wherein, R 2for the alkylidene group of C2-C12 or the arylidene of C6-C14, be preferably the alkylidene group of C2-C8, phenylene or biphenylene.Preferred, described diamines is quadrol, propylene diamine, 1,6-hexanediamine, Ursol D, O-Phenylene Diamine and 4, at least one in 4 '-benzidine.
Described vulcabond can for being dissolved in the vulcabond of the various routines in described lubricating base oil, and its general formula can be OCN-R 3-NCO, wherein, R 3can be the arylidene of the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or C6-C30, be preferably xylylene or hexylidene between xylene, methylenediphenyl, sub-dicyclohexylmethyl, Asia.Preferred, described vulcabond is at least one in tolylene diisocyanate, methylenediphenyl diisocyanates, hexamethylene vulcabond, dicyclohexylmethyl vulcabond and an xylylene diisocyanate.
In more preferably embodiment, the specific operation process of step (1) comprising:
(1-1) mixed with vulcabond by lubricating base oil and be heated to 50-60 DEG C, then adding diamines, be warming up to 80 DEG C, reaction 20-30 minute, obtains intermediate product;
(1-2) lubricating base oil mixed with monoamine and be heated to 50-60 DEG C, the mixture obtained being added in above-mentioned intermediate product, reaction 20-30 minute after mixing, and the product obtained after reaction is warming up to 200-220 DEG C, and insulation refining 1-30 minute;
(1-3) mixture obtained in step (1-2) is mixed with lubricating base oil, obtain the lubricating grease that temperature is 95-105 DEG C, and by this lubricating grease three-roll grinder grinding 1-3 time.
In above-mentioned preferred implementation, the amount of the lubricating base oil used separately in step (1-1), step (1-2) and step (1-3) can account for the 10-50 % by weight of the lubricating base oil gross weight used in step (1), is preferably 20-45 % by weight.And the lubricating base oil used separately in step (1-1), step (1-2) and step (1-3) can be identical or different.
In step (2), the catalytic condition of lipid acid of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6 can comprise: temperature of reaction is 40-90 DEG C, and the reaction times is 20-120 minute.
Under preferable case, the ratio of the integral molar quantity of the lipid acid of described higher fatty acid and described binary aromatic acid and described C1-C6 is 1: 0.1-10, is more preferably 1: 0.2-5; And the mol ratio of the lipid acid of described binary aromatic acid and described C1-C6 is 1: 0.1-2, is more preferably 1: 0.2-0.8.
Under preferable case, the ratio of the integral molar quantity of the carboxyl in the lipid acid of the molar weight of calcium hydroxide and the carboxyl in the carboxyl in described higher fatty acid, described binary aromatic acid and described C1-C6 is 0.4-0.6: 1, is more preferably 0.5-0.55: 1.
The lipid acid of described higher fatty acid, described binary aromatic acid and described C1-C6 all with describe above identical.
In a preferred embodiment, the specific operation process of step (2) can comprise:
(2-1a) by the aqueous solution of lubricating base oil and calcium hydroxide, add the lipid acid of binary aromatic acid and C1-C6, reaction 10-15 minute, be warming up to 80-90 DEG C, add higher fatty acid, be uniformly mixed 20-30 minute, be warming up to 105-110 DEG C and dewater, be then warming up to 200-220 DEG C and insulation refining 1-30 minute;
(2-2a) mixture obtained in step (2-1a) is mixed with lubricating base oil, obtain the lubricating grease that temperature is 100-120 DEG C, and by this lubricating grease three-roll grinder grinding 1-3 time.
Wherein, the amount of the lubricating base oil used in step (2-1a) can account for the 50-80 % by weight of the lubricating base oil gross weight used in step (2); The amount of the lubricating base oil used in step (2-2a) can account for the 20-50 % by weight of the lubricating base oil gross weight used in step (2).
In another kind of preferred implementation, the specific operation process of step (2) can comprise:
(2-1b) lipid acid of lubricating base oil with higher fatty acid, binary aromatic acid and C1-C6 is mixed, be warming up to 80-90 DEG C, add calcium hydroxide aqueous solution, be uniformly mixed 40-60 minute, be warming up to 105-110 DEG C to dewater, be then warming up to 200-220 DEG C and insulation refining 1-30 minute;
(2-2b) mixture obtained in step (2-1a) is mixed with lubricating base oil, obtain the lubricating grease that temperature is 100-120 DEG C, and by this lubricating grease three-roll grinder grinding 1-3 time.
Wherein, the amount of the lubricating base oil used in step (2-1b) can account for the 50-80 % by weight of the lubricating base oil gross weight used in step (2); The amount of the lubricating base oil used in step (2-2b) can account for the 20-50 % by weight of the lubricating base oil gross weight used in step (2).
Method according to the present invention, relative to total consumption of the described lubricating base oil of 100 weight parts, total consumption of vulcabond, diamines and monoamine in step (1) can be 0.5-22 weight part, is preferably 3-15 weight part; Total consumption of the lipid acid of calcium hydroxide, higher fatty acid, binary aromatic acid and C1-C6 in step (2) can be 2.2-36 weight part, is preferably 5-25 weight part.And the consumption of lubricating base oil can account for the 30-70 % by weight of total consumption of lubricating base oil in whole preparation process in step (1); In step (2), the consumption of lubricating base oil can account for the 30-70 % by weight of total consumption of grease base oil in whole preparation process.In addition, step (3) also can add a certain amount of lubricating base oil, to adjust the correlated performance of the lubricating grease of final preparation, in step (3), the add-on of lubricating base oil can account for the 0-30 % by weight of total consumption of grease base oil in whole preparation process.Described lubricating base oil is identical with above-described.
The preparation method of composite calcium-base four polyurea grease according to the present invention can also be included at least one step in step (1)-step (3) other the various additives adding this area routine and use, and described additive can be such as at least one in extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent.Relative to total consumption of the described lubricating base oil of 100 weight parts, total consumption of described extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent can be 0.1-15 % by weight, is preferably 0.5-10 weight part.Described extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent are all identical with above-described separately.
The invention will be further described by the following examples.
The separation method of four polyureas: first by lubricating grease sherwood oil (boiling point 60-90 DEG C) washing, filtration is precipitated, and the dilute acetic acid solution precipitated with 5 % by weight is soaked 5-10 minute and stirred, filters, filter residue use water cleans, then uses the NaHCO of 1 % by weight 3solution soaking, filters, and when being 7 by the cleaning of filter residue water to filtrate pH value, the precipitation obtained being carried out drying, obtains four polyureas.
Embodiment 1
The present embodiment is for illustration of described composite calcium-base four polyurea grease provided by the invention and preparation method thereof.
(1) four polyurea greases are prepared
Feed composition: (purchased from Exxon Mobil chemical company, 100 DEG C of viscosity are 11mm to HVI500SN base oil 2/ s): 435g; Stearylamine (purchased from ACROS company): 31.87g; Quadrol: 3.56g; 4,4 '-diphenylmethanediisocyanate (purchased from ACROS company, MDI): 29.57g;
First by the HVI500SN base oil of 150g and 29.57g MDI Hybrid Heating to 50 DEG C, slowly add 3.56g quadrol, be warming up to 80 DEG C, react 30 minutes, obtain mixture A1; 150gHVI500SN base oil is mixed with 31.87g stearylamine, be heated to 60 DEG C, and add in mixture A1, be warming up to 80 DEG C, react 30 minutes, continue to be warming up to 210 DEG C, then add 135g HVI500SN base oil and be cooled to 100 DEG C, then grind 2 times with three-roll grinder, obtain four polyurea greases.
(2) complex calcium lubricating grease is prepared
Feed composition: (purchased from Exxon Mobil chemical company, 100 DEG C of viscosity are 11mm to HVI500SN base oil 2/ s): 427.5g; Terephthalic acid: 29.05g; Acetic acid: 5.25g; Ca (OH) 2: 19.11g; 12-oxystearic acid (purchased from prestige Ninghua, Tongliao City work limited liability company): 23.7g;
In 280g HVI500SN base oil, add the lime milk solution containing 19.11g calcium hydroxide, add 29.05g terephthalic acid and 5.25g acetic acid, react 10 minutes, be warming up to 80 DEG C, add 23.7g12-oxystearic acid, be uniformly mixed 30 minutes, be warming up to 105 DEG C, after finished off water, be warming up to 210 DEG C, keep 10 minutes, add 147.5g HVI500SN base oil, be cooled to 120 DEG C, then grind 2 times with three-roll grinder, obtain complex calcium lubricating grease.
(3) composite calcium-base four polyurea grease is prepared
Four polyurea greases obtained above getting and each 200g mixing of complex calcium lubricating grease, 400g altogether, and add 3g tungsten disulfide, 5g Selenium Sulfide, 5g fluorographite, 3g di-iso-octyldiphenylamine and 5g zinc naphthenate, after using mixing machine to mix 5 minutes, carry out circulating filtration, homogenizing, degassed successively, obtain composite calcium-base four polyurea grease.
Can calculate according to material and learn, the composition of the lubricating grease of so preparation as: lubricating base oil accounts for 82.0 % by weight, and four polyureas account for 6.2 % by weight, and calcium complex soap accounts for 6.8 % by weight, and other additives account for 5.0 % by weight.
From described composite calcium-base four polyurea grease, isolate four polyureas, and isolated four polyureas are carried out infrared analysis, nuclear magnetic resonance spectroscopy and Electrospray Ionization Mass Spectrometry respectively, obtain spectrogram as shown in Figure 1-Figure 3.As can be seen from Figure 1,3310cm -1~ 3323cm -1the peak at place is the stretching vibration absorption peak of-NH-in four polyureas molecules, 1630cm -1the peak at place is the vibration absorption peak of-CO-in four polyureas molecules; As can be seen from Figure 2, the peak of about δ=155HZ is the chemical shift of-CO-in four polyureas molecules; As can be seen from Figure 3, the mass-to-charge ratio of sample is 1100.4m/z, and the relative molecular mass of this and four polyureas matches.Therefore, can be determined by the spectral data of Fig. 1-Fig. 3, the molecular structural formula of four polyureas in this composite calcium-base four polyurea grease is as follows.
Comparative example 1
Composite calcium-base four polyurea grease is prepared according to the method for embodiment 1, difference is, prepare in the process of complex calcium lubricating grease in step (2), replace terephthalic acid with the acetic acid of 2 times of molar weights, thus obtained composite calcium-base four polyurea grease.
Comparative example 2
Prepare composite calcium-base polyurea grease according to the method for embodiment 1, difference is, in the process preparing polyurea grease, do not add quadrol, thus obtained composite calcium-base two polyurea grease.
Comparative example 3
Composite calcium-base four polyurea grease is prepared according to the method for embodiment 1, difference is, prepare in the process of complex calcium lubricating grease in step (2), replace terephthalic acid with the phenylformic acid of 2 times of molar weights, thus obtained composite calcium-base four polyurea grease.
Embodiment 2
The present embodiment is for illustration of described composite calcium-base four polyurea grease provided by the invention and preparation method thereof.
Composite calcium-base four polyurea grease is prepared according to the method for embodiment 1, difference is, prepare in the process of complex calcium lubricating grease in step (2), replace terephthalic acid with the m-phthalic acid of same molar, thus obtained composite calcium-base four polyurea grease.
Embodiment 3
The present embodiment is for illustration of described composite calcium-base four polyurea grease provided by the invention and preparation method thereof.
Composite calcium-base four polyurea grease is prepared according to the method for embodiment 1, difference is, other additives are not added in step (3), as tungsten disulfide, Selenium Sulfide, fluorographite, di-iso-octyldiphenylamine and zinc naphthenate, thus obtained composite calcium-base four polyurea grease.
Embodiment 4
The present embodiment is for illustration of described composite calcium-base four polyurea grease provided by the invention and preparation method thereof.
(1) four polyurea greases are prepared
Feed composition: (purchased from China National Offshore Oil Corporation (CNOOC), 100 DEG C of viscosity are 12mm to naphthene base crude oil 2/ s): 469.6g; Amino dodecane (purchased from ACROS company): 13.49g; 1,6-hexanediamine (purchased from ACROS company): 4.23g; Tolylene diisocyanate (purchased from ACROS company, TDI): 12.68g;
First by the naphthene base crude oil of 150g and 12.68gTDI Hybrid Heating to 50 DEG C, slowly add 4.23g 1,6-hexanediamine, be warming up to 80 DEG C, react 30 minutes, obtain mixture B1; 150g naphthene base crude oil is mixed with 13.49g amino dodecane, is heated to 60 DEG C, and add in mixture B1, be warming up to 80 DEG C, react 30 minutes, continue to be warming up to 210 DEG C, add 169.6g naphthene base crude oil again and be cooled to 100 DEG C, then grind 2 times with three-roll grinder, obtain four polyurea greases.
(2) complex calcium lubricating grease is prepared
Feed composition: (purchased from China National Offshore Oil Corporation (CNOOC), 100 DEG C of viscosity are 12mm to naphthene base crude oil 2/ s): 345g; 4,4 '-biphenyl dicarboxylic acid (purchased from ACROS company): 96.80g; Butyric acid: 7.83g; Ca (OH) 2: 36.63g; Eicosyl carboxylic acid (purchased from ACROS company): 31.25g;
In 245g naphthene base crude oil, add the lime milk solution containing 36.63g calcium hydroxide, add 96.80g4,4 '-biphenyl dicarboxylic acid, react 10 minutes, be warming up to 80 DEG C, add 31.25g eicosyl carboxylic acid, be uniformly mixed 30 minutes, be warming up to 105 DEG C, after finished off water, be warming up to 210 DEG C, keep 10 minutes, add 100g naphthene base crude oil, be cooled to 120 DEG C, then grind 2 times with three-roll grinder, obtain complex calcium lubricating grease.
(3) composite calcium-base four polyurea grease is prepared
Four polyurea greases obtained above getting and each 200g mixing of complex calcium lubricating grease, 400g altogether, and add 1g tungsten disulfide, 1g Selenium Sulfide, 1g calcium carbonate, 1g di-iso-octyldiphenylamine and 1g barium mahogany sulfonate, after using mixing machine to mix 5 minutes, carry out circulating filtration, homogenizing, degassed successively, obtain composite calcium-base four polyurea grease.
Can calculate according to material and learn, the composition of the lubricating grease of so preparation as: lubricating base oil accounts for 80.5 % by weight, and four polyureas account for 3.0 % by weight, and calcium complex soap accounts for 15.3 % by weight, and other additives account for 1.2 % by weight.
Embodiment 5
The present embodiment is for illustration of described composite calcium-base four polyurea grease provided by the invention and preparation method thereof.
(1) four polyurea greases are prepared
Feed composition: (purchased from Exxon Mobil chemical company, 100 DEG C of kinematic viscosity are 10mm to poly alpha olefine synthetic oil PAO 10 2/ s): 355.5g; Para-totuidine (purchased from ACORS company): 12.97g; 4,4 '-benzidine (purchased from ACORS company): 11.16g; Hexamethylene diisocyanate (purchased from ACROS company, HMDI): 20.37g;
First by the poly alpha olefine synthetic oil PAO 10 of 120g with 20.37g HMDI Hybrid Heating to 50 DEG C, slowly add 11.16g 4,4 '-benzidine, be warming up to 80 DEG C, react 30 minutes, obtain mixture C 1; 120g poly alpha olefine synthetic oil PAO 10 is mixed with 12.97g para-totuidine, be heated to 60 DEG C, and add in mixture C 1, be warming up to 80 DEG C, react 30 minutes, continue to be warming up to 210 DEG C, then add 115.5g poly alpha olefine synthetic oil PAO 10 and be cooled to 100 DEG C, then grind 2 times with three-roll grinder, obtain four polyurea greases.
(2) complex calcium lubricating grease is prepared
Feed composition: (100 DEG C of kinematic viscosity are 10mm to poly alpha olefine synthetic oil PAO 10 2/ s, purchased from Exxon Mobil chemical company): 463g; 4,4 '-biphenyl dicarboxylic acid (purchased from ACROS company): 4.11g; Oxalic acid: 1.17; Ca (OH) 2: 7.4g; Lauric acid (purchased from ACROS company): 28g;
In 280g poly alpha olefine synthetic oil PAO 10, add the lime milk solution containing 7.4g calcium hydroxide, add 4.11g 4,4 '-biphenyl dicarboxylic acid and 1.17g oxalic acid, react 10 minutes, be warming up to 80 DEG C, add 28g lauric acid, be uniformly mixed 30 minutes, be warming up to 105 DEG C, after finished off water, be warming up to 210 DEG C, keep 10 minutes, add 183g poly alpha olefine synthetic oil PAO 10, be cooled to 120 DEG C, then grind 2 times with three-roll grinder, obtain complex calcium lubricating grease.
(3) composite calcium-base four polyurea grease is prepared
Four polyurea greases obtained above getting and each 200g mixing of complex calcium lubricating grease, 400g altogether, and add 1g tungsten disulfide, 1g Selenium Sulfide, 1g calcium carbonate, 1g di-iso-octyldiphenylamine and 1g barium mahogany sulfonate, after using mixing machine to mix 5 minutes, carry out circulating filtration, homogenizing, degassed successively, obtain composite calcium-base four polyurea grease.
Can calculate according to material and learn, the composition of the lubricating grease of so preparation as: lubricating base oil accounts for 86.5 % by weight, and four polyureas account for 8.6 % by weight, and calcium complex soap accounts for 3.7 % by weight, and other additives account for 1.2 % by weight.
Test case
(1) dropping point of various different lubricating grease is detected according to the method for GB/T 3498-2008;
(2) detect the Drawing cone in-degree of various different lubricating grease according to the method for GB/T 269-1991 and extend Drawing cone in-degree;
(3) the copper corrosion performance of various different lubricating grease is detected according to the method for GB/T 7326-1987;
(4) Stencil oil-dividing of various different lubricating grease is detected according to the method for SH/T 0324-1992;
(5) the water pouring number of dropouts of various different lubricating grease is detected according to the method for SH/T 0109-2004;
(6) P of various different lubricating grease is detected according to the method for SH/T 0202-1992 b, P dand wear scar diameter;
(7) respectively hardening test is carried out to various different lubricating grease according to the method for SH/T 0370-1995, to detect their resistance hardening energy;
Above-mentioned detected result is as shown in table 1 below.
Table 1
As can be seen from the data of table 1, composite calcium-base four polyurea grease according to the present invention overcomes the problem of the sclerosis that conventional complex calcium lubricating grease exists, and properties is all better, shows excellent over-all properties.Particularly, the Drawing cone in-degree difference of described composite calcium-base four polyurea grease of the present invention, front and back cone penetration difference of hardening, Stencil oil-dividing and water pouring number of dropouts are all obviously less, thus show excellent mechanical stability, colloid stability and anti-water drenching energy.

Claims (27)

1. composite calcium-base four polyurea grease, is characterized in that, this lubricating grease contains lubricating base oil, four polyureas and calcium complex soap, and described calcium complex soap is the mixture of the fatty acid calcium of higher fatty acid calcium, binary aromatic acid calcium and C1-C6; In described calcium complex soap, the ratio of the integral molar quantity of the fatty acid calcium of the molar weight of higher fatty acid calcium and binary aromatic acid calcium and C1-C6 is 1:0.1-10, and the mol ratio of the fatty acid calcium of binary aromatic acid calcium and C1-C6 is 1:0.1-2; Relative to the described lubricating base oil of 100 weight parts, the content of described four polyureas is 0.5-22 weight part, and the content of described calcium complex soap is 2.2-36 weight part; Described calcium complex soap is the saponification reaction product of the lipid acid of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6; The structural formula of described binary aromatic acid such as formula shown in (I),
Wherein, R 2, R 3, R 4, R 5and R 6in one be carboxyl, the alkyl of C1-C5 of carboxyl substituted or the aryl of the C6-C12 of carboxyl substituted, R 2, R 3, R 4, R 5and R 6in other four be the fluorinated aryl of hydrogen, the alkyl of C1-C5, the thiazolinyl of C2-C5, the alkynyl of C2-C5, the aryl of C6-C12, the fluoro-alkyl of C1-C5 or C6-C12 independently of one another.
2. lubricating grease according to claim 1, wherein, in described calcium complex soap, the ratio of the integral molar quantity of the fatty acid calcium of the molar weight of higher fatty acid calcium and binary aromatic acid calcium and C1-C6 is 1:0.2-5, and the mol ratio of the fatty acid calcium of binary aromatic acid calcium and C1-C6 is 1:0.2-0.8.
3. lubricating grease according to claim 1, wherein, described higher fatty acid is the straight chain fatty acid of C12-C24 or the hydroxy fatty acid of C12-C24.
4. lubricating grease according to claim 3, wherein, described higher fatty acid is be selected from least one in lauric acid, oleic acid, palmitinic acid, stearic acid, 12-oxystearic acid and eicosyl carboxylic acid.
5. lubricating grease according to claim 1, wherein, in formula (I), R 2, R 3, R 4, R 5and R 6in one be the phenyl of carboxyl, carboxymethyl or carboxyl substituted, R 2, R 3, R 4, R 5and R 6in other four be the alkyl of hydrogen or C1-C2 independently of one another.
6. lubricating grease according to claim 1 or 5, wherein, described binary aromatic acid is at least one in phthalic acid, m-phthalic acid, terephthalic acid and biphenyl dicarboxylic acid.
7. lubricating grease according to claim 1, wherein, the lipid acid of described C1-C6 is at least one in acetic acid, propionic acid, butyric acid and oxalic acid.
8. lubricating grease according to claim 1, wherein, described four polyureas are the compound shown in formula (II),
Wherein, each R 1independently selected from alkyl, cycloalkyl or aryl, R 2be selected from alkylidene group or arylidene, each R 3independently selected from alkylidene group, cycloalkylidene or arylidene.
9. lubricating grease according to claim 8, wherein, each R 1independently selected from the alkyl of C8-C24, the cycloalkyl of C8-C24 or C6-C10 aryl, R 2be selected from the alkylidene group of C2-C12 or the arylidene of C6-C14, each R 3independently selected from the arylidene of the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or C6-C30.
10. lubricating grease according to claim 9, wherein, each R 1the phenyl replaced independently selected from the alkyl of the cycloalkyl of the alkyl of C10-C18, C10-C18, phenyl, C1-C3 or the phenyl of halogen substiuted, R 2be selected from the alkylidene group of C2-C8, phenylene or biphenylene, each R 3independently selected from xylylene or hexylidene between xylene, methylenediphenyl, sub-dicyclohexylmethyl, Asia.
11. lubricating grease according to claim 1, wherein, described lubricating base oil is at least one in mineral oil, vegetables oil and synthetic oil.
12. lubricating grease according to claim 1 and 2, wherein, described lubricating grease is also containing at least one in extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent.
13. lubricating grease according to claim 12, wherein, relative to the described lubricating base oil of 100 weight parts, the total content of described extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent is 0.1-15 weight part.
14. lubricating grease according to claim 12, wherein, described extreme pressure anti-wear additives is at least one in dithio Acidic phosphates zinc, dithio dialkyl amido zinc formate, triphenylphosphorothionate, organic molybdenum complex compound, olefine sulfide, molybdenumdisulphide, tetrafluoroethylene, thiophosphoric acid molybdenum, clorafin, dibutyl dithiocaarbamate antimony, tungsten disulfide, Selenium Sulfide, fluorographite, calcium carbonate and zinc oxide; Described oxidation inhibitor is at least one in the amino p-cresol of pentanoic, di-iso-octyldiphenylamine, phenyl-a-naphthylamine, 2,6 ditertiary butyl p cresol and 2,6-di-t-butyl-alpha, alpha-dimethyl; Described rust-preventive agent is at least one in barium mahogany sulfonate, petroleum sodium sulfonate, benzothiazole, benzotriazole, zinc naphthenate and alkenyl succinic acid.
The preparation method of 15. 1 kinds of composite calcium-base four polyurea greases, the method comprises the following steps:
(1) under the existence of lubricating base oil, by vulcabond, diamines and monoamine contact reacts, heat up the mixture obtained after reaction refining, and wherein, the mol ratio of vulcabond, diamines and monoamine is (1.9-2.1): 1:(1.9-2.1);
(2) under the existence of lubricating base oil, by the lipid acid contact reacts of calcium hydroxide and higher fatty acid, binary aromatic acid and C1-C6, the mixture obtained is carried out intensifications dewater after reaction;
(3) the product mixing that product step (1) obtained and step (2) obtain;
Wherein, the ratio of the integral molar quantity of the lipid acid of the molar weight of higher fatty acid and binary aromatic acid and C1-C6 is 1:0.1-10, and the mol ratio of the lipid acid of binary aromatic acid and C1-C6 is 1:0.1-2;
Wherein, the specific operation process of step (1) comprising:
(1-1) mixed with vulcabond by lubricating base oil and be heated to 50-60 DEG C, then adding diamines, be warming up to 80 DEG C, reaction 20-30 minute, obtains intermediate product;
(1-2) lubricating base oil mixed with monoamine and be heated to 50-60 DEG C, the mixture obtained being added in above-mentioned intermediate product, reaction 20-30 minute after mixing, and the product obtained after reaction is warming up to 200-220 DEG C, and insulation refining 1-30 minute;
(1-3) mixture obtained in step (1-2) is mixed with lubricating base oil, obtain the lubricating grease that temperature is 95-105 DEG C, and by this lubricating grease three-roll grinder grinding 1-3 time.
16. methods according to claim 15, wherein, in step (1), the mol ratio of vulcabond, diamines and monoamine is 2:1:2.
17. methods according to claim 15 or 16, wherein, the general formula of described monoamine is R 1nH 2, wherein, R 1for the alkyl of C8-C24, the cycloalkyl of C8-C24 or C6-C10 aryl.
18. methods according to claim 17, wherein, described monoamine is at least one in aniline, m-chloro aniline, p-Chlorobenzoic acid amide, para-totuidine, amino dodecane, tetradecy lamine, cetylamine and stearylamine.
19. methods according to claim 15 or 16, wherein, the general formula of described diamines is NH 2-R 2-NH 2, wherein, R 2for the alkylidene group of C2-C12 or the arylidene of C6-C14.
20. methods according to claim 19, wherein, described diamines is quadrol, propylene diamine, 1,6-hexanediamine, Ursol D, O-Phenylene Diamine and 4, at least one in 4 '-benzidine.
21. methods according to claim 15 or 16, wherein, the general formula of described vulcabond is OCN-R 3-NCO, wherein, R 3for the arylidene of the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or C6-C30.
22. methods according to claim 21, wherein, described vulcabond is at least one in tolylene diisocyanate, methylenediphenyl diisocyanates, hexamethylene vulcabond, dicyclohexylmethyl vulcabond and an xylylene diisocyanate.
23. methods according to claim 15, wherein, in step (2), described catalytic condition comprises: temperature of reaction is 40-90 DEG C, and the reaction times is 20-120 minute.
24. methods according to claim 15, wherein, relative to total consumption of the described lubricating base oil of 100 weight parts, total consumption of vulcabond, diamines and monoamine in step (1) is 0.5-22 weight part, and total consumption of the lipid acid of calcium hydroxide, higher fatty acid, binary aromatic acid and C1-C6 in step (2) is 2.2-36 weight part.
25. methods according to claim 15, wherein, the ratio of the integral molar quantity of the lipid acid of the molar weight of higher fatty acid and binary aromatic acid and C1-C6 is 1:0.2-5, and the mol ratio of the lipid acid of binary aromatic acid and C1-C6 is 1:0.2-0.8.
26. methods according to claim 15 or 24, wherein, described method is also included at least one step in step (1)-step (3) at least one added in extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent.
27. methods according to claim 26, wherein, relative to total consumption of the described lubricating base oil of 100 weight parts, total consumption of described extreme pressure anti-wear additives, oxidation inhibitor and rust-preventive agent is 0.1-15 weight part.
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