CN103289785A - Composite calcium-base octa-polyurea lubricating grease and preparation method thereo - Google Patents
Composite calcium-base octa-polyurea lubricating grease and preparation method thereo Download PDFInfo
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- CN103289785A CN103289785A CN2012100420121A CN201210042012A CN103289785A CN 103289785 A CN103289785 A CN 103289785A CN 2012100420121 A CN2012100420121 A CN 2012100420121A CN 201210042012 A CN201210042012 A CN 201210042012A CN 103289785 A CN103289785 A CN 103289785A
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Abstract
The invention also relates to a composite calcium-base octa-polyurea lubricating grease and a preparation method thereof. The preparation method comprises the following steps: (1) in the presence of lubricating base oil, carrying out contact reaction on the calcium hydroxide, higher fatty acid and binary aromatic acid, heating to dehydrate the reaction mixture, and cooling to 50-70 DEG C to obtain a composite calcium-base lubricating grease; and (2) adding diisocyanate, diamine and monoamine into the composite calcium-base lubricating grease, carrying out contact reaction at 80-120 DEG C, and heating the reaction mixture for refinement, wherein the diisocyanate:diamine:monoamine mol ratio is (3.9-4.1):(2.9-3.1):2. The composite calcium-base octa-polyurea lubricating grease provided by the invention has excellent comprehensive properties.
Description
Technical field
The present invention relates to a kind of preparation method of composite calcium-base eight polyurea greases, and by composite calcium-base eight polyurea greases of this method preparation.
Background technology
Polyurea grease (abbreviation polyurea grease) is by the prepared lubricating grease of organic compound multiviscosisty base oil that contains urea groups in the molecule.Because polyurea thickening agent is different from metal soap base viscosifying agent, metal ion not, avoided in the soap base viscosifying agent metal ion to the catalysed oxidn of grease base oil, therefore polyurea grease has good oxidative stability and thermostability, makes polyurea grease be more suitable for lubricating in hot conditions.
At present, the report of article and patent mainly concentrates on preparation and the synthetic aspect of two polyurea greases, and two polyurea grease shear stabilities are relatively poor, work 100,000 times with 60 cone penetration differences of work all at 80 more than the unit.To the report of eight polyurea greases seldom.Salient featuress such as the dropping point of eight polyurea greases, extreme pressure property, colloid stability, oxidation stability increase than existing two polyurea greases.Therefore have excellent lubrication fat performance more, and can obtain using widely.Yet, because the shear stability of eight polyurea greases is not good, thereby limited its application under the working condition of high temperature, high speed and heavy loading.
Complex calcium lubricating grease is the high dropping point grease of developing the earliest, be a kind of heatproof, withstand voltage, broad-spectrum good lubricating grease, have good mechanical stability, colloid stability and anti-water drenching energy, but the sclerosis problem is its widely used lethal factor of restriction, and improve the sclerosis problem is the main contents of 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, for example, CN1364859A and CN1657599A disclose respectively by introduce the calcium base polyurea grease that two polyureas obtain in complex calcium lubricating grease, yet the over-all properties of these calcium base polyurea greases is not good.
Summary of the invention
The objective of the invention is provides a kind of new composite calcium-base eight polyurea greases and preparation method thereof in order to overcome the above-mentioned defective that existing lubricating grease exists.
The invention provides a kind of preparation method of composite calcium-base eight polyurea greases, this method may further comprise the steps:
(1) in the presence of lubricating base oil, with calcium hydroxide, higher fatty acid and binary aromatic acid contact reacts, with the dehydration that heats up of the mixture that obtains after the reaction, be cooled to 50-70 ℃ then, obtain complex calcium lubricating grease;
(2) in described complex calcium lubricating grease, add vulcabond, diamines and monoamine, under 80-120 ℃, carry out contact reacts, and the mixture that will obtain after will reacting intensification refining, wherein, the mol ratio of the consumption of vulcabond, diamines and monoamine is (3.9-4.1): (2.9-3.1): 2.
The invention provides composite calcium-base eight polyurea greases by method for preparing.
Prepared according to the methods of the invention composite calcium-base eight polyurea greases have excellent comprehensive performances.Concrete, in described composite calcium-base eight polyurea greases, by introducing eight polyureas, overcome the problem of the sclerosis of traditional complex calcium lubricating grease existence; By introducing the mixture of higher fatty acid calcium and binary aromatic acid calcium, overcome the over-all properties defect of bad that traditional polyurea grease exists.
And, with compare as the composite calcium-base polyurea grease of composite calcium-base viscosifying agent by the mixture of introducing higher fatty acid calcium and monobasic aromatic acid calcium, described composite calcium-base polyurea grease has obviously more excellent over-all properties, particularly has more excellent mechanical stability, colloid stability and anti-water drenching energy.
In addition, method according to the present invention, by preparing complex calcium lubricating grease earlier, in complex calcium lubricating grease, prepare eight polyureas then, thereby realized in a reactor, finishing the preparation of composite calcium-base eight polyurea grease products, but also avoided causing easily in the preparation process of conventional composite calcium-base polyurea grease the problem of the strong volatilization of small molecules acid.
Other features and advantages of the present invention will partly be described in detail in embodiment subsequently.
Description of drawings
Fig. 1 is the infrared analysis spectrogram of eight polyureas in the lubricating grease of embodiment 1 preparation;
Fig. 2 is the nuclear magnetic resonance spectroscopy spectrogram of eight polyureas in the lubricating grease of embodiment 1 preparation;
Fig. 3 is the electrospray ionization mass spectrum analysis of spectra of eight polyureas in the lubricating grease of embodiment 1 preparation.
Embodiment
The invention provides a kind of preparation method of composite calcium-base eight polyurea greases, this method may further comprise the steps:
(1) in the presence of lubricating base oil, with calcium hydroxide, higher fatty acid and binary aromatic acid contact reacts, with the dehydration that heats up of the mixture that obtains after the reaction, be cooled to 50-70 ℃ (being preferably 50-60 ℃) then, obtain complex calcium lubricating grease;
(2) in described complex calcium lubricating grease, add vulcabond, diamines and monoamine, under 80-120 ℃, carry out contact reacts, and the mixture that will obtain after will reacting intensification refining, wherein, the mol ratio of the consumption of vulcabond, diamines and monoamine is (3.9-4.1): (2.9-3.1): 2.
In step (1), calcium hydroxide, higher fatty acid and the catalytic condition of binary aromatic acid can comprise: temperature of reaction is 80-90 ℃, and the reaction times is 10-60 minute.
In one embodiment, the specific operation process of step (1) can comprise: with the aqueous solution of lubricating base oil and calcium hydroxide, add the binary aromatic acid, reacted 10-15 minute, be warming up to 80-90 ℃, add higher fatty acid, mixed 20-30 minute, be warming up to 105-110 ℃ and dewater, be cooled to 50-70 ℃ then.
In another embodiment, the specific operation process of step (1) can comprise: lubricating base oil is mixed with higher fatty acid and binary aromatic acid, be warming up to 80-90 ℃, add calcium hydroxide aqueous solution, mixed 40-60 minute, be warming up to 105-110 ℃ and dewater, be cooled to 50-70 ℃ then.
Under the preferable case, the ratio of the carboxyl in the molar weight of calcium hydroxide and the described higher fatty acid and the integral molar quantity of the carboxyl in the binary aromatic acid is 0.4-0.6: 1, and 0.5-0.55 more preferably: 1.
Under the preferable case, the mol ratio of described higher fatty acid and described binary aromatic acid is 1: 0.1-10, more preferably 1: 0.2-5.
Described higher fatty acid can for example can be the straight chain fatty acid of C12-C24 or the hydroxy fatty acid of C12-C24 for the conventional higher fatty acid that uses in this area.Preferably, described higher fatty acid is to be selected from least a in lauric acid, oleic acid, palmitinic acid, stearic acid, 12-oxystearic acid and the eicosyl carboxylic acid.
The structural formula of described binary aromatic acid is preferably suc as formula shown in (I),
Wherein, R
2, R
3, R
4, R
5And R
6In one be the aryl of the C6-C12 of the alkyl of C1-C5 of carboxyl, carboxyl substituted or carboxyl substituted, R
2, R
3, R
4, R
5And R
6In other four be the alkyl of hydrogen, C1-C5, the thiazolinyl of C2-C5, the alkynyl of C2-C5, the aryl of C6-C12, the fluoro-alkyl of C1-C5 or the fluorinated aryl of C6-C12 independently of one another.
Under the 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 a in phthalic acid, m-phthalic acid, terephthalic acid and the biphenyl dicarboxylic acid (as 4,4 '-biphenyl dicarboxylic acid).
Most preferably, described binary aromatic acid be terephthalic acid and/or 4,4 '-biphenyl dicarboxylic acid.
In step (2), the condition of described refining can comprise: temperature is 200-220 ℃, and the time is 1-30 minute.
In a kind of preferred implementation, in described complex calcium lubricating grease, add vulcabond, diamines and monoamine and under 80-120 ℃, carry out catalytic process and preferably include: described complex calcium lubricating grease and vulcabond are mixed, then add diamines, be warming up to 80-90 ℃ of reaction 10-40 minute, then add monoamine, and under 80-90 ℃, reacted 10-40 minute, be warming up to 100-120 ℃ then and kept 10-40 minute down.
In above-mentioned preferred implementation, monoamine preferably adds with the form of the mixture of monoamine and lubricating base oil.The mixture of described monoamine and lubricating base oil is preferably by mixing monoamine with lubricating base oil, be heated to 50-60 ℃ and make then.
In above-mentioned preferred implementation, vulcabond can add separately, also can add with the form of the mixture of vulcabond and lubricating base oil.The mixture of described vulcabond and lubricating base oil can be by mixing vulcabond with lubricating base oil, be heated to 50-60 ℃ and make then.
Method according to the present invention, in step (2), the mol ratio of the consumption of vulcabond, diamines and monoamine most preferably is 4: 3: 2.
The general formula of described monoamine can be R
1NH
2, wherein, R
1Can be the alkyl of C8-C24, cycloalkyl or the C6-C10 aryl of C8-C24.In the present invention, the alkyl of described C8-C24 can be to replace or unsubstituted alkyl, and substituting group can be halogen, for example Cl, Br usually; The cycloalkyl of described C8-C24 can be to replace or unsubstituted cycloalkyl, and substituting group can be halogen, for example Cl, Br usually; Described C6-C10 aryl can be to replace or unsubstituted aryl, and substituting group can be the alkyl of halogen (for example Cl, Br), C1-C5 usually.Under the preferable case, R
1The phenyl that the phenyl that replaces for the alkyl of the cycloalkyl of the alkyl of C10-C18, C10-C18, phenyl, C1-C3 or halogen (for example Cl, Br) replace.Preferred, described monoamine is at least a in aniline, m-chloro aniline, p-Chlorobenzoic acid amide, para-totuidine, amino dodecane, tetradecy lamine, cetylamine and the stearylamine.
The general formula of described diamines can be NH
2-R
2-NH
2, wherein, R
2Be the alkylidene group of C2-C12 or the arylidene of C6-C14, be preferably alkylidene group, phenylene or the biphenylene of C2-C8.Preferred, described diamines is quadrol, propylene diamine, 1,6-hexanediamine, Ursol D, O-Phenylene Diamine and 4, at least a in 4 '-benzidine.
Described vulcabond can be for being dissolved in the vulcabond of the various routines in the described lubricating base oil, and its general formula can be OCN-R
3-NCO, wherein, R
3Can be the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or the arylidene of C6-C30, be preferably xylylene or hexylidene between methylene phenyl, methylenediphenyl, inferior dicyclohexyl methyl, Asia.Preferred, described vulcabond is at least a in tolylene diisocyanate, methylenediphenyl diisocyanates, hexamethylene vulcabond, dicyclohexyl methyl vulcabond and the xylylene vulcabond.
Method according to the present invention, with respect to the consumption of the described lubricating base oil of 100 weight parts, total consumption of the calcium hydroxide in the step (1), higher fatty acid and binary aromatic acid can be the 2.2-36 weight part, is preferably the 5-25 weight part; Total consumption of vulcabond, diamines and monoamine in the step (2) can be the 0.5-22 weight part, is preferably the 3-15 weight part.
Method according to the present invention, described lubricating base oil can all add in step (1), also can add a part of lubricating base oil in step (1), adds another part lubricating base oil in step (2).
Under the preferable case, be benchmark with total consumption of lubricating base oil described in the whole process of preparation, in step (1), add the lubricating base oil of 50-70 weight %, the lubricating base oil of adding 30-50 weight % in step (2).Concrete, lubricating base oil can add by at least a mode in following three kinds of modes in the step (2): a) monoamine is dissolved in the lubricating base oil, adds lubricating base oil in the process that adds monoamine; B) vulcabond is dissolved in the lubricating base oil, in the process that adds vulcabond, adds lubricating base oil; C) after finishing refining, the lubricating grease that refining is obtained naturally cools to 145-155 ℃, adds lubricating base oil then and carries out chilling, to be cooled to below 120 ℃, is preferably 100-120 ℃.Further preferably, the lubricating base oil that a) mode passed through adds accounts for the 5-50 weight % of the total consumption of lubricating base oil in the step (2), pass through b) lubricating base oil that adds of mode accounts for the 0-50 weight % of the total consumption of lubricating base oil in the step (2), passes through c) lubricating base oil that adds of mode accounts for the 50-95 weight % of the total consumption of lubricating base oil in the step (2).
In the present invention, described lubricating base oil can be 2-150mm for 100 ℃ of viscosity for example for the conventional various lubricating base oils that use in this area
2/ s (is preferably 2-100mm
2/ s, more preferably 8-50mm
2/ s) lubricating base oil.Concrete, what described lubricating base oil for example can be in mineral oil, vegetables oil and the synthetic oil is at least a.Described synthetic oil can be poly-a-olefin oil (PAO), ester class oil, alkyl-silicone oil, Fischer-Tropsch synthesis oil etc.
Method according to the present invention can also be included in and add conventional other the various additives that use in this area in step (1) and/or the step (2), and what described additive for example can be in extreme pressure anti-wear additives, oxidation inhibitor and the rust-preventive agent is at least a.With respect to the 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 preferably the 0.5-10 weight part for 0.1-15 weight %.
Described extreme pressure anti-wear additives for example can be in dithio dialkyl group zinc phosphate, dithio dialkyl amido zinc formate, triphenyl thiophosphatephosphorothioate, organic molybdenum complex compound, olefine sulfide, molybdenumdisulphide, tetrafluoroethylene, thiophosphoric acid molybdenum, clorafin, dibutyl dithiocaarbamate antimony, tungsten disulfide, Selenium Sulfide, fluorographite, calcium carbonate and the zinc oxide at least a.
Described oxidation inhibitor is preferably the arylamine kind antioxidant, and what described arylamine kind antioxidant for example can be 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 is at least a.
Described rust-preventive agent for example can be in barium mahogany sulfonate, petroleum sodium sulfonate, benzene a pair of horses going side by side thiazole, benzotriazole, zinc naphthenate and the alkenyl succinic acid at least a.
The present invention also provides composite calcium-base eight polyurea greases by method for preparing.Described composite calcium-base eight polyurea greases have excellent comprehensive performances, particularly have more excellent mechanical stability, colloid stability and anti-water drenching energy.
The invention will be further described by the following examples.
The separation method of eight polyureas: earlier lubricating grease is used sherwood oil (boiling point 60-90 ℃) washing, filtration obtains precipitation, with dilute acetic acid solution immersion 5-10 minute and the stirring of precipitation with 5 weight %, filters, and the filter residue water cleans, and uses the NaHCO of 1 weight % again
3Solution soaking is filtered, with the filter residue water clean to filtrate pH value be 7 o'clock, the precipitation that obtains is carried out drying, namely get eight polyureas.
Embodiment 1
Present embodiment is used for explanation described composite calcium-base eight polyurea greases of the present invention and preparation method thereof.
Feed composition: (100 ℃ of viscosity are 11mm to the HVI500SN base oil
2/ s is available from Exxon Mobil chemical company): 861g; Stearylamine (available from ACROS company): 20.39g; Quadrol: 6.81g; 4,4 '-diphenylmethanediisocyanate is (available from ACROS company, MDI): 37.80g; Terephthalic acid: 34.3g; Ca (OH)
2: 21g; 12-oxystearic acid (available from prestige Ninghua, Tongliao City worker limited liability company): 23.7g; Tungsten disulfide: 7.5g; Selenium Sulfide: 12.5g; Fluorographite: 12.5g; Di-iso-octyldiphenylamine: 7.5g; Zinc naphthenate: 12.5g.
500g HVI500SN base oil is mixed with 23.7g 12-oxystearic acid and 34.3g terephthalic acid, stir, be warming up to 80 ℃, to wherein dripping the lime milk solution that contains 21g calcium hydroxide, stir fast saponification 60 minutes, be warming up to 105 ℃, taken off water after, be cooled to 50 ℃, obtain complex calcium lubricating grease.In described complex calcium lubricating grease, add 37.80g MDI, be heated to 50 ℃, stirred 10 minutes, add the 6.81g quadrol, be warming up to 85 ℃, reacted 30 minutes, obtain mixture A1; 20.39g stearylamine and 150g HVI500SN base oil are mixed, be heated to 50 ℃, and add among the mixture A1, and 85 ℃ of following isothermal reactions 30 minutes, be warming up to 110 ℃ afterwards and kept 30 minutes; Then, be warming up to 210 ℃, kept 10 minutes, naturally cool to 150 ℃, add the 211gHVI500SN base oil afterwards again, treat to add 7.5g tungsten disulfide, 12.5g Selenium Sulfide, 12.5g fluorographite, 7.5g di-iso-octyldiphenylamine and 12.5g zinc naphthenate when temperature is cooled to 110 ℃, after stirring, carry out circulating filtration, homogenizing, the degassing successively, obtain composite calcium-base eight polyurea greases.
From described composite calcium-base eight polyurea greases, isolate eight polyureas, and isolated eight polyureas are carried out infrared analysis, nuclear magnetic resonance spectroscopy and electrospray ionization mass spectrum analysis 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 in the eight polyureas molecules-the stretching vibration absorption peak of NH-, and 1630cm
-1The peak at place is in the eight polyureas molecules-vibration absorption peak of CO-; As can be seen from Figure 2, the peak about δ=155HZ is in the eight polyureas molecules-chemical shift of CO-; As can be seen from Figure 3, the mass-to-charge ratio of sample is 1721.4m/z, and the relative molecular mass of this and eight polyureas matches.Therefore, can be determined by the spectral data of Fig. 1-Fig. 3 that the molecular structural formula of eight polyureas in these composite calcium-base eight polyurea greases is as follows.
Comparative Examples 1
Method according to embodiment 1 prepares composite calcium-base eight polyurea greases, and difference is with the acetic acid replacement terephthalic acid of 2 times of molar weights, thereby to make composite calcium-base eight polyurea greases.
Comparative Examples 2
Method according to embodiment 1 prepares the composite calcium-base polyurea grease, and difference is not add quadrol, thereby make composite calcium-base two polyurea greases.
Comparative Examples 3
Method according to embodiment 1 prepares composite calcium-base eight polyurea greases, and difference is with the phenylformic acid replacement terephthalic acid of 2 times of molar weights, thereby to make composite calcium-base eight polyurea greases.
Embodiment 2
Present embodiment is used for explanation described composite calcium-base eight polyurea greases of the present invention and preparation method thereof.
Method according to embodiment 1 prepares composite calcium-base eight polyurea greases, and difference is with the m-phthalic acid replacement terephthalic acid of same molar, thereby to make composite calcium-base eight polyurea greases.
Embodiment 3
Present embodiment is used for explanation described composite calcium-base eight polyurea greases of the present invention and preparation method thereof.
Method according to embodiment 1 prepares composite calcium-base eight polyurea greases, and difference is, does not add other additives, as tungsten disulfide, Selenium Sulfide, fluorographite, di-iso-octyldiphenylamine and zinc naphthenate, thereby makes composite calcium-base eight polyurea greases.
Embodiment 4
Present embodiment is used for explanation described composite calcium-base eight polyurea greases of the present invention and preparation method thereof.
Feed composition: (available from China National Offshore Oil Corporation (CNOOC), 100 ℃ of viscosity are 12mm to naphthene base crude oil
2/ s): 789.5g; Amino dodecane (available from ACROS company): 8g; 1,6-hexanediamine (available from ACROS company): 7.5g; Tolylene diisocyanate is (available from ACROS company, TDI): 15g; 4,4 '-biphenyl dicarboxylic acid (available from ACROS company): 118.58g; Ca (OH)
2: 40g; Eicosyl carboxylic acid (available from ACROS company): 31.25g; Tungsten disulfide: 2.5g; Selenium Sulfide: 2.5g; Calcium carbonate: 2.5g; Di-iso-octyldiphenylamine: 2.5g; Barium mahogany sulfonate: 2.5g;
The 450g naphthene base crude oil is mixed with the lime milk solution that contains 40g calcium hydroxide, stir, to wherein adding 118.58g 4,4 '-biphenyl dicarboxylic acid, reacted 15 minutes, be warming up to 85 ℃, add eicosyl carboxylic acid 31.25g, saponification 20 minutes, be warming up to 110 ℃, after having taken off water, be cooled to 60 ℃, obtain complex calcium lubricating grease.15g TDI is mixed with the 100g naphthene base crude oil, be heated to 50 ℃, and join in the described complex calcium lubricating grease, mixed 10 minutes, add 7.5g 1, the 6-hexanediamine is warming up to 80 ℃, reacts 30 minutes, obtains mixture B1; 8g amino dodecane and 100g naphthene base crude oil are mixed, be heated to 50 ℃, and add among the mixture B1, and 80 ℃ of following isothermal reactions 35 minutes, be warming up to 100 ℃ afterwards and kept 35 minutes; Then, be warming up to 220 ℃, kept 10 minutes, naturally cool to 150 ℃, add the 139.5g naphthene base crude oil afterwards again, treat to add 2.5g tungsten disulfide, 2.5g Selenium Sulfide, 2.5g calcium carbonate, 2.5g di-iso-octyldiphenylamine and 2.5g barium mahogany sulfonate when temperature is cooled to 110 ℃, after stirring, carry out circulating filtration, homogenizing, the degassing successively, obtain composite calcium-base eight polyurea greases.
Embodiment 5
Present embodiment is used for explanation described composite calcium-base eight polyurea greases of the present invention and preparation method thereof.
(100 ℃ of kinematic viscosity are 10mm to feed composition: poly alpha olefine synthetic oil PAO 10
2/ s is available from Exxon Mobil chemical company): 814.5g; Para-totuidine (available from ACROS company): 21.50g; 4,4 '-benzidine (available from ACROS company): 55.47g; Hexamethylene diisocyanate is (available from ACROS company, HMDI): 67.53g; 4,4 '-biphenyl dicarboxylic acid (available from ACROS company): 7.26g; Ca (OH)
2: 7.4g; Lauric acid (available from ACROS company): 28g; Tungsten disulfide: 2.5g; Selenium Sulfide: 2.5g; Calcium carbonate: 2.5g; Di-iso-octyldiphenylamine: 2.5g; Barium mahogany sulfonate: 2.5g;
500g poly alpha olefine synthetic oil PAO 10 is mixed with the lime milk solution that contains 7.4g calcium hydroxide, stir, to wherein adding 7.26g 4,4 '-biphenyl dicarboxylic acid, reacted 15 minutes, be warming up to 90 ℃, add lauric acid 28g, saponification 10 minutes, be warming up to 120 ℃, after having taken off water, be cooled to 55 ℃, obtain complex calcium lubricating grease.In described complex calcium lubricating grease, add 67.53g HMDI, be heated to 50 ℃, obtain mixture C 1; 29.96g para-totuidine and 100g poly alpha olefine synthetic oil PAO 10 are mixed, stirred 10 minutes, add 55.47g 4,4 '-benzidine is warming up to 90 ℃, reacts 20 minutes, obtains mixture C 1; 21.50g para-totuidine and 150g poly alpha olefine synthetic oil PAO 10 are mixed, be heated to 50 ℃, and add in the mixture C 1,90 ℃ of following isothermal reactions 20 minutes, be warming up to 120 ℃ afterwards and kept 20 minutes; Then, be warming up to 200 ℃, kept 20 minutes, naturally cool to 150 ℃, add 164.5g poly alpha olefine synthetic oil PAO 10 afterwards again, treat to add 2.5g tungsten disulfide, 2.5g Selenium Sulfide, 2.5g calcium carbonate, 2.5g di-iso-octyldiphenylamine and 2.5g barium mahogany sulfonate when temperature is cooled to 110 ℃, after stirring, carry out circulating filtration, homogenizing, the degassing successively, obtain composite calcium-base eight polyurea greases.
Test case
(1) detects the dropping point of various lubricating grease according to the method for GB/T 3498-2008;
(2) method according to GB/T 269-1991 detects the Drawing cone in-degree of various lubricating grease and prolongs the Drawing cone in-degree;
(3) detect the copper corrosion performance of various lubricating grease according to the method for GB/T 7326-1987;
(4) detect the Stencil oil-dividing of various lubricating grease according to the method for SH/T 0324-1992;
(5) water that detects various lubricating grease according to the method for SH/T 0109-2004 drenches number of dropouts;
(6) detect the P of various lubricating grease according to the method for SH/T 0202-1992
B, P
DAnd wear scar diameter;
(7) according to the method for SH/T 0370-1995 respectively to the test of hardening of various lubricating grease, to detect their resistance hardening energy;
Above-mentioned detected result is as shown in table 1 below.
Table 1
By the data of table 1 as can be seen, composite calcium-base eight polyurea greases according to the present invention have overcome the problem of the sclerosis that conventional complex calcium lubricating grease exists, and every performance is all better, shows the excellent comprehensive performance.Particularly, it is all obviously less that cone penetration difference, Stencil oil-dividing and water drench number of dropouts before and after the Drawing cone in-degree difference of prepared according to the methods of the invention composite calcium-base eight polyurea greases, the sclerosis, thereby show excellent mechanical stability, colloid stability and anti-water drenching energy.
Claims (24)
1. the preparation method of composite calcium-base eight polyurea greases, this method may further comprise the steps:
(1) in the presence of lubricating base oil, with calcium hydroxide, higher fatty acid and binary aromatic acid contact reacts, with the dehydration that heats up of the mixture that obtains after the reaction, be cooled to 50-70 ℃ then, obtain complex calcium lubricating grease;
(2) in described complex calcium lubricating grease, add vulcabond, diamines and monoamine, under 80-120 ℃, carry out contact reacts, and the mixture that will obtain after will reacting intensification refining, wherein, the mol ratio of the consumption of vulcabond, diamines and monoamine is (3.9-4.1): (2.9-3.1): 2.
2. method according to claim 1, wherein, in step (1), described catalytic condition comprises: temperature of reaction is 80-90 ℃, the reaction times is 10-60 minute.
3. method according to claim 1, wherein, the ratio of the carboxyl in the molar weight of calcium hydroxide and the described higher fatty acid and the integral molar quantity of the carboxyl in the binary aromatic acid is 0.4-0.6: 1.
4. according to claim 1 or 3 described methods, wherein, the mol ratio of described higher fatty acid and described binary aromatic acid is 1: 0.1-10.
5. method according to claim 4, wherein, the mol ratio of described higher fatty acid and described binary aromatic acid is 1: 0.2-5.
6. according to any described method in the claim 1,3 and 5, wherein, described higher fatty acid is the straight chain fatty acid of C12-C24 or the hydroxy fatty acid of C12-C24.
7. method according to claim 6, wherein, described higher fatty acid is to be selected from least a in lauric acid, oleic acid, palmitinic acid, stearic acid, 12-oxystearic acid and the eicosyl carboxylic acid.
8. according to any described method in the claim 1,3 and 5, wherein, the structural formula of described binary aromatic acid is suc as formula shown in (I),
Wherein, R
2, R
3, R
4, R
5And R
6In one be the aryl of the C6-C12 of the alkyl of C1-C5 of carboxyl, carboxyl substituted or carboxyl substituted, R
2, R
3, R
4, R
5And R
6In other four be the alkyl of hydrogen, C1-C5, the thiazolinyl of C2-C5, the alkynyl of C2-C5, the aryl of C6-C12, the fluoro-alkyl of C1-C5 or the fluorinated aryl of C6-C12 independently of one another.
9. method according to claim 8, 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.
10. method according to claim 8, wherein, described binary aromatic acid is at least a in phthalic acid, m-phthalic acid, terephthalic acid and the biphenyl dicarboxylic acid.
11. method according to claim 1, wherein, in step (2), the condition of described refining comprises: temperature is 200-220 ℃, and the time is 1-30 minute.
12. according to claim 1 or 11 described methods, wherein, in step (2), in described complex calcium lubricating grease, add vulcabond, diamines and monoamine and under 80-120 ℃, carry out catalytic process and comprise: described complex calcium lubricating grease and vulcabond are mixed, then add diamines, be warming up to 80-90 ℃ of reaction 10-40 minute, then add monoamine, and under 80-90 ℃, reacted 10-40 minute, be warming up to 100-120 ℃ then and kept 10-40 minute down.
13. method according to claim 1, wherein, the mol ratio of the consumption of vulcabond, diamines and monoamine is 4: 3: 2.
14. according to claim 1 or 13 described methods, wherein, the general formula of described monoamine is R
1NH
2, wherein, R
1Be the alkyl of C8-C24, cycloalkyl or the C6-C10 aryl of C8-C24.
15. method according to claim 14, wherein, described monoamine is at least a in aniline, m-chloro aniline, p-Chlorobenzoic acid amide, para-totuidine, amino dodecane, tetradecy lamine, cetylamine and the stearylamine.
16. according to claim 1 or 13 described methods, wherein, the general formula of described diamines is NH
2-R
2-NH
2, wherein, R
2Be the alkylidene group of C2-C12 or the arylidene of C6-C14.
17. method according to claim 16, wherein, described diamines is quadrol, propylene diamine, 1,6-hexanediamine, Ursol D, O-Phenylene Diamine and 4, at least a in 4 '-benzidine.
18. according to claim 1 or 13 described methods, wherein, the general formula of described vulcabond is OCN-R
3-NCO, wherein, R
3Be the alkylidene group of C6-C30, the cycloalkylidene of C6-C30 or the arylidene of C6-C30.
19. method according to claim 18, wherein, described vulcabond is at least a in tolylene diisocyanate, methylenediphenyl diisocyanates, hexamethylene vulcabond, dicyclohexyl methyl vulcabond and the xylylene vulcabond.
20. according to any described method in the claim 1,3,5 and 13, wherein, consumption with respect to the described lubricating base oil of 100 weight parts, total consumption of the calcium hydroxide in the step (1), higher fatty acid and binary aromatic acid is the 2.2-36 weight part, and total consumption of vulcabond, diamines and monoamine in the step (2) is the 0.5-22 weight part.
21. method according to claim 1, wherein, described method also is included in and adds at least a in extreme pressure anti-wear additives, oxidation inhibitor and the rust-preventive agent in step (1) and/or the step (2).
22. method according to claim 21, wherein, with respect to the 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 the 0.1-15 weight part.
23. according to claim 21 or 22 described methods, wherein, described extreme pressure anti-wear additives is at least a in dithio dialkyl group zinc phosphate, dithio dialkyl amido zinc formate, triphenyl thiophosphatephosphorothioate, organic molybdenum complex compound, olefine sulfide, molybdenumdisulphide, tetrafluoroethylene, thiophosphoric acid molybdenum, clorafin, dibutyl dithiocaarbamate antimony, tungsten disulfide, Selenium Sulfide, fluorographite, calcium carbonate and the zinc oxide; Described oxidation inhibitor is at least a 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 a in barium mahogany sulfonate, petroleum sodium sulfonate, benzene a pair of horses going side by side thiazole, benzotriazole, zinc naphthenate and the alkenyl succinic acid.
24. composite calcium-base eight polyurea greases by any described method preparation among the claim 1-23.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104513700A (en) * | 2013-09-30 | 2015-04-15 | 中国石油化工股份有限公司 | Composite calcium-zirconium-based octa-polyurea lubricating grease and preparation method thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3243372A (en) * | 1961-01-24 | 1966-03-29 | Chevron Res | Greases thickened with polyurea |
| CN85108714A (en) * | 1985-11-22 | 1987-06-03 | 中国石油化工总公司一坪化工厂 | Composition of composite alkaling earth metal base grease and preparation method thereof |
| CN1493673A (en) * | 2002-10-30 | 2004-05-05 | 中国石油化工股份有限公司 | Preparation method of polyurea-composite calcium lubricating grease |
-
2012
- 2012-02-22 CN CN201210042012.1A patent/CN103289785B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3243372A (en) * | 1961-01-24 | 1966-03-29 | Chevron Res | Greases thickened with polyurea |
| CN85108714A (en) * | 1985-11-22 | 1987-06-03 | 中国石油化工总公司一坪化工厂 | Composition of composite alkaling earth metal base grease and preparation method thereof |
| CN1493673A (en) * | 2002-10-30 | 2004-05-05 | 中国石油化工股份有限公司 | Preparation method of polyurea-composite calcium lubricating grease |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104513700A (en) * | 2013-09-30 | 2015-04-15 | 中国石油化工股份有限公司 | Composite calcium-zirconium-based octa-polyurea lubricating grease and preparation method thereof |
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