A kind of compound lithium base grease composite and preparation method thereof
Technical field
The present invention relates to a kind of compound lithium base grease composite and preparation method thereof.
Background technology
Railway grease is one of staple product of industrial lubricants; It is a kind ofly to have plastic solid to semi-solid lubricant by what viscosifying agent and base oil were formed; For satisfying harsh application conditions, often add various functional additives and improve its performance and be widely used in iron and steel, automobile, aerospace and war industry.Complex lithium grease is one type of high-performance grease product being processed as viscosifying agent by the compound lithium soap of 12-oxystearic acid and diprotic acid; Because of it has good mechanical stability; The bearing wastage is few; Outstanding water-resistant antirust and oxidation stability have application widely in industries such as Iron And Steel Industry, automotive industrys.
DOP (DOP) has good mixing property, and plasticizing efficiency is high, and volatility is lower; Advantages such as low-temperature pliability is better, and electric property is high, and thermotolerance and weathering resistance are good; In industry, be used widely, be mainly used in the auxiliary agent or the raw material of industries such as coating, film, cable.
The low-temperature performance of compositing lithio ester that with MO is base oil is relatively poor, and because it contains organic acids and base usually, so easily lubricating component is caused corrosion.With the viscous silicone fluid be the compositing lithio ester of base oil because its lubricity is relatively poor, thereby can not be used for the lubricated of precision instrument.
It is the high-performance composite grease sulphonate lubricating grease and preparation method thereof of raw material with the Octyl adipate that CN101824357A discloses a kind of, and this patent is to utilize Octyl adipate to be used for high-performance composite grease sulphonate lubricating grease as base oil.
In the research of above lithium soap grease and since the relatively poor decisions in aspect such as high temperature performance, oxidative stability, lubricity its can not be in the use in high-end lubricated fields such as precision meter, aviation.
DOP uses in high-end lubricated field as a kind of synthetic oil, like lubricating of fields such as precision meter, aviation.
Summary of the invention
The objective of the invention is to overcome the deficiency of prior art, a kind of compsn of new complex lithium grease is provided.
Another object of the present invention provides the preparation of compositions method of above-mentioned complex lithium grease.
A kind of compound lithium base grease composite, be made up of the material of following weight percentage: grease base oil 75%-85%, viscosifying agent 12%-20%, additive 0.1%-3%, said grease base oil are DOP (DOP).
In the above-mentioned compound lithium base grease composite, said viscosifying agent is the mixture of 12-oxystearic acid lithium salts and sebacic acid lithium salts, and the mass ratio of described 12-oxystearic acid lithium salts and sebacic acid lithium salts is 1:2 ~ 2:1.
In the above-mentioned compound lithium base grease composite; Said additive is the mixture of two kinds of inhibitor, extreme pressure anti-wear additives, sanitas, rust-preventive agent etc. or three kinds; Wherein the mass percent of inhibitor is 0.01%-3%; The ratio of extreme pressure anti-wear additives is 0.01%-0.1%, and the ratio of sanitas is 0.01%-0.1%, and the mass percent of rust-preventive agent is 0.01%-1%.
In the above-mentioned compound lithium base grease composite, described inhibitor is one or more in pentanoic, di-iso-octyldiphenylamine, phenolic ester type oxidation inhibitor, the oxidation inhibitor 618.
In the above-mentioned compound lithium base grease composite, described extreme pressure anti-wear additives is one or more in clorafin, titanium oxide, dibutyl dithiocaarbamate oxygen molybdenum, the molybdenumdisulphide.
In the above-mentioned compound lithium base grease composite, described rust-preventive agent is one or more in barium mahogany sulfonate, synthetic sodium sulfonate, the zinc naphthenate.
The preparation method of above-mentioned compound lithium base grease composite is characterized in that comprising the steps:
(1) with in the middle of 12-oxystearic acid, sebacic acid, the grease base oil adding reactor drum, be adjusted to temperature A, heated and stirred dissolving back adds the hot strong solution of Lithium Hydroxide MonoHydrate and carries out saponification;
(2) intensification is dewatered, and carries out high temperature puffing afterwards;
(3) add to remain under certain temperature behind the additive and stir, the system of treating naturally cools to room temperature and obtains product.
Among the above-mentioned preparation method, step (1) saponification temperature is 90 ℃-120 ℃; The described dehydration temperaturre of step (2) is 130 ℃-150 ℃, and swelling temperature is 170 ℃-190 ℃; The said temperature of step (3) is 110 ℃-130 ℃.
Compared with prior art, the present invention has following beneficial effect: complex lithium grease of the present invention is a grease base oil with the DOP, makes full use of characteristics such as the ester oil high temperature performance is good, oxidative stability is good, lubricity excellence; Adopt compound lithium base metal soap base to carry out the single stage method multiviscosisty, method is simply practiced thrift production energy consumption; Product possesses good colloid stability and mechanical stability; Contain the performance that inhibitor possesses work under certain high temperature; And the adding through extreme pressure anti-wear additives makes compound lithium base grease composite possess excellent extreme pressure anti-wear, can extensively in engineering machinery field, use.
Embodiment
Below in conjunction with embodiment the present invention is done further explanation, but protection scope of the present invention is not limited to the scope that embodiment representes.
Embodiment 1:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification, will be warming up to 140 ℃ then and dewater, under 200 ℃, carry out expanded after dehydration is accomplished; Treat will be dissolved with the base oil adding of 618,0.25 kilogram of titanium oxide of 0.5 kilogram of oxidation inhibitor and 0.25 kilogram of barium mahogany sulfonate and keep stirring after the expanded end, system naturally cools to room temperature and obtains product.
Embodiment 2:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification; To be warming up to 140 ℃ then dewaters; Dehydration is accomplished the back and under 200 ℃, is carried out expandedly, and the base oil of treating will to be dissolved with after the expanded end 0.5 kilogram of pentanoic, 0.25 kilogram of dibutyl dithiocaarbamate oxygen molybdenum and 0.25 kilogram of barium mahogany sulfonate adds and keeps stirring, and system naturally cools to room temperature and obtains product.
Embodiment 3:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification, will be warming up to 140 ℃ then and dewater, under 200 ℃, carry out expanded after dehydration is accomplished; Treat will be dissolved with the base oil adding of 0.5 kilogram of di-iso-octyldiphenylamine, 0.25 kilogram of clorafin and 0.25 kilogram of barium mahogany sulfonate and keep stirring after the expanded end, system naturally cools to room temperature and obtains product.
Embodiment 4:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification, will be warming up to 140 ℃ then and dewater, under 200 ℃, carry out expanded after dehydration is accomplished; Treat will be dissolved with the base oil adding of 0.5 kilogram of phenolic ester type oxidation inhibitor, 0.25 kilogram of titanium oxide and 0.25 kilogram of synthetic sodium sulfonate and keep stirring after the expanded end, system naturally cools to room temperature and obtains product.
Embodiment 5:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification, will be warming up to 140 ℃ then and dewater, under 200 ℃, carry out expanded after dehydration is accomplished; Treat will be dissolved with the base oil adding of 618,0.25 kilogram of molybdenumdisulphide of 0.5 kilogram of oxidation inhibitor and 0.25 kilogram of synthetic sodium sulfonate and keep stirring after the expanded end, system naturally cools to room temperature and obtains product.
Embodiment 6:
In the middle of 10 kilograms of 12-oxystearic acids and 80 kilograms of DOP of 5 kilograms of sebacic acid addings; 100 ℃ of following heated and stirred; Treat that two kinds of lipid acid dissolving backs add the hot strong solution of Lithium Hydroxide MonoHydrate and carry out saponification; To be warming up to 140 ℃ then dewaters; Dehydration is accomplished the back and under 200 ℃, is carried out expandedly, and the base oil of treating will to be dissolved with after the expanded end 0.5 kilogram of phenolic ester type oxidation inhibitor, 0.25 kilogram of dibutyl dithiocaarbamate oxygen molybdenum and 0.25 kilogram of zinc naphthenate adds and keeps stirring, and system naturally cools to room temperature and obtains product.
The product performance contrast of each embodiment is as shown in table 1
Table 1:
Project |
Embodiment 1 |
Embodiment 2 |
Embodiment 3 |
Embodiment 4 |
Embodiment 5 |
Embodiment 6 |
Characterizing method |
Cone penetration/0.1mm |
256 |
263 |
260 |
265 |
258 |
255 |
GB/T 269-91 |
Dropping point/℃ |
295 |
>300 |
296 |
290 |
>300 |
297 |
GB/T 4929-85(91) |
Stencil oil-dividing/% |
0.72 |
0.85 |
0.79 |
0.88 |
0.75 |
0.90 |
SH/T 0324-92 |
Moisture/% |
Trace |
Trace |
Trace |
Trace |
Trace |
Trace |
GB/T 512-65(90) |