CN1683480A - Process for preparing lubricating oil additive containing nano microparticles - Google Patents

Process for preparing lubricating oil additive containing nano microparticles Download PDF

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CN1683480A
CN1683480A CN 200410031184 CN200410031184A CN1683480A CN 1683480 A CN1683480 A CN 1683480A CN 200410031184 CN200410031184 CN 200410031184 CN 200410031184 A CN200410031184 A CN 200410031184A CN 1683480 A CN1683480 A CN 1683480A
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salt
consumption
alkali
microemulsion
acid
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CN100338200C (en
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徐风华
韦淡平
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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 preparation process of lubricating oil additive containing nanometer particle includes the following steps: 1) mixing metal salt or acid solution with lubricant oil dispersant, emulsifier and base oil, heating to 30-120 deg.c and dropping co-dispersant until the microemulsion becomes clear and transparent to obtain the salt or acid microemulsion; 2) mixing alkali in the same equivalent to the salt or acid in the above said microemulsion with with dispersant, emulsifier and base oil, heating to 30-120 deg.c and dropping co-dispersant until the microemulsion becomes clear and transparent to obtain the alkali microemulsion; and 3) mixing the two said kinds of microemulsion at 25-100 deg.c through stirring at 100-2000 rpm for 0.5-8 hr to obtain the product. The present invention produces nanometer particle directly in lubricant oil and the obtained additive has excellent stability and extreme pressure wear resistance in base oil.

Description

The preparation process lubricant oil additive that contains nanoparticle
Technical field
Preparation process lubricant oil additive of the present invention specifically, is the preparation method who contains the lubrication oil anti-wear extreme pressure additive of nanoparticle.
Technical background
Past, the research that nanotechnology is used to improve the lubricating oil extreme pressure anti-wear obtained tangible progress for over ten years.From the kind of additive, can be divided into Inorganic Nanometer Antiwear Agents, the organic and inorganic matrix material anti-wear agent of finishing, and ashless nano antiwear agent.Inorganic Nanometer Antiwear Agents generally adopts two-step approach, promptly utilizes various physics and chemical process to prepare the ultra-fine grain of metal, metal oxide, metallic sulfide etc., they is distributed in the base oil as additive goes again.Many metal oxides such as Lithium Oxide 98min, zirconium white, titanium oxide and silicon oxide etc., very high fusing point and hardness are arranged itself, it is the presoma of preparation pottery, be used for the anti-caking power that lubricating oil can significantly improve lubricating oil, and the nanometer superfine powder body of preparation can not resemble the problem that has easy oxidation the metal powder.Introduced the good result that nano size rare earth hydroxide has obtained as lubricating oil additive among the CN1218103A; US6,243,669 have introduced the natural crystal that will contain multiple metal oxide handles the nanometer state, adds after the specific catalyst as lubricating oil additive again, but does not introduce anti-wear effect in detail.CN1362500A has introduced mixture with a kind of borate and ester as lubricating oil additive, does not also introduce anti-wear effect.The problem that above-mentioned additive all exists nanoparticle to reunite.
Summary of the invention
The invention provides the preparation method of the lubrication oil anti-wear extreme pressure additive that contains nanoparticle, this method directly generates nanoparticle in lubricating oil, and nanoparticle is remained among the liquid pearl of microemulsion of high dispersing, avoid reunion, and then avoided the solid-liquid separation problem that causes because of reunion.
Preparation process lubricant oil additive provided by the invention comprises following three kinds of methods:
First method comprises:
1) with metal-salt or acid solution and lubricating oil dispersant, emulsifying agent, base oil mixes, and is heated to 30 ℃~120 ℃, drips dispersion aids to the microemulsion clear, obtains the microemulsion of salt or acid;
2) will with the salt in the above-mentioned microemulsion or the alkali of sour equivalent, mix with dispersion agent, emulsifying agent and base oil, be heated to 30 ℃~120 ℃, drip dispersion aids to the microemulsion clear, obtain alkaline microemulsion;
3) above-mentioned two kinds of microemulsions being mixed, is 25 ℃~100 ℃ in temperature, and stir speed (S.S.) is to stir 0.5~8 hour under 100~2000 rev/mins the condition, obtains final product.
Specifically, first method can be carried out according to following steps:
Step 1: with metal-salt or acid solution and lubricating oil dispersant, emulsifying agent, base oil mixes, and stirs, and is heated to 30 ℃~120 ℃, and preferred 40 ℃~100 ℃, drip dispersion aids to the microemulsion clear, obtain the microemulsion of salt or acid.
Wherein, said metal-salt or acid are water-soluble zirconates, water-soluble aluminum salt, boric acid or their mixture, preferred zirconium tetrachloride, tri-chlorination zirconium, aluminum chloride, aluminum nitrate, boric acid, and the concentration of the aqueous solution is 5~20%, preferred 8~15%.
Said lubricating oil dispersant is allyl butyrate imide, petroleum sodium sulfonate, calcium mahogany sulfonate or their mixture.
Said dispersion aids is an alcohols, as: Pentyl alcohol, n-hexyl alcohol, n-dodecanol or their mixture.
Said emulsifying agent is (Si Ben-60), sorbitol monooleate (Si Ben-80), polyoxyethylene (20) sorbitol anhydride mono-laurate (tween 20), polyoxyethylene sorbitan monoleate (tween-80) or their mixture.
Said base oil is mineral oil, ucon oil, vegetables oil or their mixture.40 ℃ of viscosity of mineral oil, ucon oil, vegetables oil are 5~50mm 2/ s, preferred 20~40mm 2/ s.Ucon oil is ester class oil, polyethers, synthetic hydrocarbon or their mixture.Vegetables oil is Oleum Gossypii semen, rapeseed oil, peanut oil or their mixture.
Weight in metal-salt or acid solution is 1 part, and the consumption of base oil is 10~40 parts, preferred 20~30 parts; The consumption of lubricating oil dispersant is 1~6 part, preferred 2~4 parts; The consumption of emulsifying agent is 1~6 part, preferred 2~4 parts;
Step 2: will with the alkali of above-mentioned salt or sour equivalent, mix with dispersion agent, emulsifying agent and base oil, stir, be heated to 30 ℃~120 ℃, drip dispersion aids to the microemulsion clear, obtain alkaline microemulsion.
Said alkali can be organic bases or mineral alkali, and organic bases is C2~C16 alkylamine or polyamines polyene, or their mixture, and alkylamine can be primary amine, secondary amine or tertiary amine, as ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine etc.; Polyamines polyene can be a diethylenetriamine, triethylene tetramine, tetraethylene pentamine etc.; Mineral alkali can be sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia etc.Mineral alkali is that concentration is 1~30 weight %, preferred 8~25% the aqueous solution, and organic bases can directly use.
The implication of dispersion agent, emulsifying agent, dispersion aids and base oil is identical with step 1.
Weight in alkali or alkali lye is 1 part, and the consumption of base oil is 10~40 parts, preferred 20~30 parts; The consumption of lubricating oil dispersant is 1~6 part, preferred 2~4 parts; The consumption of emulsifying agent is 1~6 part, preferred 2~4 parts.
Step 3: above-mentioned two kinds of microemulsions are mixed, heated and stirred 0.5~8 hour, preferred 1~4 hour, stir speed (S.S.) was 100~2000 rev/mins, preferred 300~1500 rev/mins, 25 ℃~100 ℃ of Heating temperatures, obtain final product by preferred 55~80 ℃.
Second method comprises:
1), obtains the microemulsion of salt or acid with the step 1 of method one;
2) will with the salt in the above-mentioned microemulsion or the alkali of sour equivalent, the speed of dividing with 0.001~0.02mol/ joins in the above-mentioned microemulsion, in temperature is 25 ℃~100 ℃, and stir speed (S.S.) is to stir under 100~2000 rev/mins the condition to obtain final product in 0.5~8 hour.
Specifically, second method can be carried out according to following steps:
Step 1: with metal-salt or acid solution and lubricating oil dispersant, emulsifying agent, base oil mixes, and stirs, and is heated to 30 ℃~120 ℃, and preferred 40 ℃~100 ℃, drip dispersion aids to the microemulsion clear, obtain the microemulsion of salt or acid.
The implication of metal-salt or acid solution, dispersion agent, emulsifying agent, dispersion aids and base oil and consumption are identical with the step 1 of method one.
Step 2: will with the salt in the above-mentioned microemulsion or the alkali of sour equivalent, with 0.001~0.02mol/ branch, the speed that preferred 0.005~0.015mol/ divides joins in the above-mentioned microemulsion, heated and stirred 0.5~8 hour, preferred 1~4 hour, stir speed (S.S.) was 100~2000 rev/mins, preferred 300~1500 rev/mins, 25 ℃~100 ℃ of Heating temperatures, obtain final product by preferred 55 ℃~80 ℃.
Said alkali can be organic bases or mineral alkali, and organic bases is C2~C16 alkylamine or polyamines polyene, or their mixture, and alkylamine can be primary amine, secondary amine or tertiary amine, as ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine etc.; Polyamines polyene can be a diethylenetriamine, triethylene tetramine, triethylene tetramine etc.; Mineral alkali can be sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia etc.It is 1~30 weight % that mineral alkali is mixed with concentration in use, preferred 8~25% the aqueous solution, and organic bases can directly use.According to the form (liquid, solid-state or gaseous state) of alkali can take to drip, gradation adds or the mode of ventilation with 0.001~0.02mol/ branch, the speed that preferred 0.005~0.015mol/ divides joins in the microemulsion of salt or acid.
The third method comprises:
1) alkali is mixed with dispersion agent, emulsifying agent and base oil, stir, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain alkaline microemulsion to the microemulsion clear;
2) will with the metal-salt or the acid solution of alkali equivalent in the above-mentioned microemulsion, be added dropwise in the above-mentioned microemulsion with 10~60 droplets/minute speed, in temperature is 25 ℃~100 ℃, and stir speed (S.S.) is to stir 0.5~8 hour under 100~2000 rev/mins the condition, obtains final product.
Specifically, the third method can be carried out according to following steps:
Step 1: alkali is mixed with dispersion agent, emulsifying agent and base oil, stir, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain alkaline microemulsion to the microemulsion clear.
Said alkali can be organic bases or mineral alkali, and organic bases is C2~C16 alkylamine or polyamines polyene, or their mixture, and alkylamine can be primary amine, secondary amine or tertiary amine, as ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine etc.; Polyamines polyene can be a diethylenetriamine, triethylene tetramine, triethylene tetramine etc.; Mineral alkali can be sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia etc.Mineral alkali is that concentration is 1~30 weight %, preferred 8~25% the aqueous solution, and organic bases can directly use.
Said lubricating oil dispersant is allyl butyrate imide, petroleum sodium sulfonate, calcium mahogany sulfonate or their mixture.
Said dispersion aids is an alcohols, as: Pentyl alcohol, n-hexyl alcohol, n-dodecanol or their mixture.
Said emulsifying agent is (Si Ben-60), sorbitol monooleate (Si Ben-80), polyoxyethylene (20) sorbitol anhydride mono-laurate (tween 20), polyoxyethylene sorbitan monoleate (tween-80) or their mixture.
Said base oil is mineral oil, ucon oil, vegetables oil or their mixture.40 ℃ of viscosity 5~50mm of mineral oil, ucon oil, vegetables oil 2/ s, preferred 20~40mm 2/ s.Ucon oil is ester class oil, polyethers, synthetic hydrocarbon or their mixture.Vegetables oil is Oleum Gossypii semen, rapeseed oil, peanut oil or their mixture.
Weight in alkali or alkali lye is 1 part, and the consumption of base oil is 10~40 parts, preferred 20~30 parts; The consumption of lubricating oil dispersant is 1~6 part, preferred 2~4 parts; The consumption of emulsifying agent is 1~6 part, preferred 2~4 parts, obtains alkaline microemulsion.
2) will with the metal-salt or the acid solution of alkali equivalent in the above-mentioned microemulsion, with 10~60 droplets/minute, preferred 20~40 droplets/minute speed is added dropwise in the above-mentioned microemulsion, heated and stirred 0.5~8 hour, preferred 1~4 hour, stir speed (S.S.) was 100~2000 rev/mins, preferred 300~1500 rev/mins, 25 ℃~100 ℃ of Heating temperatures, obtain final product by preferred 55~80 ℃.
Said metal-salt or acid are water-soluble zirconates, water-soluble aluminum salt, boric acid or their mixture, preferred zirconium tetrachloride, tri-chlorination zirconium, aluminum chloride, aluminum nitrate, boric acid, and concentration of aqueous solution is 5~20%, preferred 8~15%.
In the lubricating oil additive according to three kinds of methods preparation provided by the invention, comprising particle diameter is the insoluble nanoparticle of 1~100nm, and these nanoparticles are reaction product of metal-salt or acid and alkali.This additive has good dispersiveness and stable in base oil, and extreme pressure, resistance to abrasion are preferably arranged.
The lubrication oil anti-wear extreme pressure additive that contains nanoparticle provided by the invention, the consumption in lubricating oil are 0.1~10 weight %.
Embodiment
Example 1
Method one
The zirconium tetrachloride aqueous solution of 2ml 13.2% is joined 1.5g Si Ben-80,1g tween 20,2g allyl butyrate imide, 25g mineral oil (40 ℃ of viscosity 22mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip Pentyl alcohol down to the microemulsion clear, 68 ℃ of Heating temperatures; Aqueous sodium hydroxide solution with 1ml 9% joins 1.5g Si Ben-80,1g tween 20,1.8g allyl butyrate imide, 25g mineral oil (40 ℃ of viscosity 22mm again 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip Pentyl alcohol down to the microemulsion clear, and Heating temperature is 89 ℃; Two kinds of microemulsions are mixed, heated and stirred is 2.5 hours under the normal pressure again, and stir speed (S.S.) is 360 rev/mins, and 55 ℃ of Heating temperatures get the clear product A, adopts the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 2
Method one
The aluminum chloride aqueous solution of 2ml 9.8% is joined 3g Si Ben-80,2g tween-80,1.6g petroleum sodium sulfonate 25g mineral oil (40 ℃ of viscosity 35.46mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-hexyl alcohol down to the microemulsion clear, and Heating temperature is 50 ℃; Sodium silicate aqueous solution with 1ml 12.5% joins 3g Si Ben-80,2g tween-80,1.6g petroleum sodium sulfonate, 25g mineral oil (40 ℃ of viscosity 35.46mm again 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-hexyl alcohol down to the microemulsion clear, and Heating temperature is 77 ℃; Two kinds of microemulsions are mixed, heated and stirred is 1.5 hours under the normal pressure again, and stir speed (S.S.) is 500 rev/mins, and Heating temperature is 73 ℃, gets the clear product B, adopts the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 3
Method one
The boric acid aqueous solution of 2ml 11.6% is joined 2g Si Ben-60,3g tween 20,2g calcium mahogany sulfonate, 25g mineral oil (40 ℃ of viscosity 40mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-hexyl alcohol down to the microemulsion clear, and Heating temperature is 42 ℃; Lithium hydroxide aqueous solution with 1ml 8.9% joins 3g Si Ben-60,2g tween 20,2g calcium mahogany sulfonate, 25g mineral oil (40 ℃ of viscosity 40mm again 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-hexyl alcohol down to the microemulsion clear, and Heating temperature is 83 ℃; Two kinds of microemulsions are mixed, heated and stirred is 3 hours under the normal pressure again, and stir speed (S.S.) is 1050 rev/mins, and 66 ℃ of Heating temperatures get the clear products C, adopts the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 4
Method two
The zirconium tetrachloride aqueous solution of 2ml 10.9% is joined 1.8g Si Ben-60,2.6g tween-80,3g thiazolinyl succinyl industry amine, 25g rapeseed oil (40 ℃ of viscosity 20.6mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip Pentyl alcohol down to the microemulsion clear, and Heating temperature is 48 ℃; The ammoniacal liquor of 1ml 24% speed with 60 droplets/minute is added dropwise in the above-mentioned microemulsion, heated and stirred is 3.5 hours under the normal pressure again, and stir speed (S.S.) is 400 rev/mins, Heating temperature is 69 ℃, get clear product D, adopt the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 5
Method three
The potassium hydroxide aqueous solution of 1ml 8.8% is joined 2.1g Si Ben-80,2.8g tween 20,2.6g allyl butyrate imide, synthetic hydrocarbon (the 40 ℃ of viscosity 35.6mm of 25g 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip Pentyl alcohol down to the microemulsion clear, and Heating temperature is 50 ℃; Again the zirconium tetrachloride aqueous solution of 2ml 11.3% speed with 30 droplets/minute is added dropwise in the above-mentioned microemulsion, heated and stirred is 2.5 hours under the normal pressure, stir speed (S.S.) is 1300 rev/mins, Heating temperature is 65 ℃, get the clear product E, adopt the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 6
Method one
The zirconium tetrachloride aqueous solution of 3ml 12.1% is joined 2.8g Si Ben-60,3.6g tween 20,1.5g petroleum sodium sulfonate, 25g Oleum Gossypii semen (40 ℃ of viscosity 22.8mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-dodecanol down to the microemulsion clear, and Heating temperature is 48 ℃; Again the 1ml di-n-butyl amine is joined 3g Si Ben-60,2g tween 20,1.5g petroleum sodium sulfonate, 25g Oleum Gossypii semen (40 ℃ of viscosity 22.8mm 2In/s) the mixture, heated and stirred is even under the normal pressure; With two kinds of liquid mixing, heated and stirred 3.5 hours, stir speed (S.S.) are 630 rev/mins again, and Heating temperature is 75 ℃, get the clear product F, adopt the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Example 7
Method two
The zirconium tetrachloride aqueous solution of 2ml10.1% is joined 6.0g Si Ben-80,4.0g tween-80,4g petroleum sodium sulfonate, 50g polyethers (40 ℃ of viscosity 30mm 2In/s) the mixture, heated and stirred is even under the normal pressure, stirs to drip n-hexyl alcohol down to the microemulsion clear, and Heating temperature is 68 ℃; The 100ml ammonia is fed in this microemulsion, and heated and stirred 1.5 hours, stir speed (S.S.) are 1 500 rev/mins, and Heating temperature is 35 ℃, get the clear product G, adopt the GB3142-82 method to measure its supporting capacity, the results are shown in Table 1.
Table 1 contains the extreme pressure and antiwear behavior of the lubricating oil of different concns additive
Numbering Form Oil film strength P B(N) Sintering load P D(N) ?????ZMZ
????1 Base oil P ????333 ????1568 ????23.65
????2 ????P+2.5‰A ????421 ????1568 ????29.90
????3 ????P+5‰A ????588 ????1568 ????37.32
????4 ????P+10‰A ????412 ????1960 ????40.05
????5 ????P+15‰A ????608 ????1960 ????45.36
????6 ????P+5‰B ????412 ????1960 ????/
????7 ????P+5‰C ????421 ????1960 ????/
????8 ????P+5‰D ????588 ????1568 ????/
????9 ????P+5‰E ????588 ????1568 ????/
????10 ????P+5‰F ????588 ????1568 ????/
????11 ????P+5‰G ????588 ????1568 ????/

Claims (22)

1. preparation method who contains the lubrication oil anti-wear extreme pressure additive of nanoparticle comprises:
1) metal-salt or acid solution are mixed with lubricating oil dispersant, emulsifying agent and lubricant base, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain the microemulsion of salt or acid to the microemulsion clear; Said metal-salt or acid are water-soluble zirconates, water-soluble aluminum salt, boric acid or their mixture; Weight in metal-salt or acid solution is 1 part, and the consumption of base oil is 10~40 parts, and the consumption of lubricating oil dispersant is 1~6 part, and the consumption of emulsifying agent is 1~6 part;
2) will mix with dispersion agent, emulsifying agent and base oil with the salt in the above-mentioned microemulsion or the alkali of sour equivalent, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain alkaline microemulsion to the microemulsion clear; Said alkali is C2~C16 alkylamine or polyamines polyene, or concentration is the aqueous solution of the mineral alkali of 1~30 weight %; Weight in alkali or alkaline solution is 1 part, and the consumption of base oil is 10~40 parts, and the consumption of lubricating oil dispersant is 1~6 part, and the consumption of emulsifying agent is 1~6 part;
3) above-mentioned two kinds of microemulsions being mixed, is 25 ℃~100 ℃ in temperature, and stir speed (S.S.) is to stir 0.5~8 hour under 100~2000 rev/mins the condition, obtains final product.
2. according to the described preparation method of claim 1, it is characterized in that said metal-salt or acid are selected from zirconium tetrachloride, tri-chlorination zirconium, aluminum chloride, aluminum nitrate, boric acid.
3. according to the described preparation method of claim 1, it is characterized in that said metal-salt or aqueous acid concentration are 5~20 weight %.
4. according to the described preparation method of claim 1, it is characterized in that, said alkali is selected from ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine, diethylenetriamine, triethylene tetramine, tetraethylene pentamine, or concentration is the aqueous solution of 8~25% sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia.
5. according to the described preparation method of claim 1, it is characterized in that, said lubricating oil dispersant is allyl butyrate imide, petroleum sodium sulfonate, calcium mahogany sulfonate or their mixture, said emulsifying agent is, sorbitol monooleate, Tween-20, polyoxyethylene sorbitan monoleate or their mixture, and said dispersion aids is Pentyl alcohol, n-hexyl alcohol, n-dodecanol or their mixture.
6. according to the described preparation method of claim 1, it is characterized in that, in the step 1, is 1 part in the weight of metal-salt or acid solution, and the consumption of base oil is 20~30 parts, and the consumption of lubricating oil dispersant is 2~4 parts, and the consumption of emulsifying agent is 2~4 parts.
7. according to the described preparation method of claim 1, it is characterized in that, in the step 2, is 1 part in the weight of alkali or alkali lye, and the consumption of base oil is 20~30 parts, and the consumption of lubricating oil dispersant is 2~4 parts, and the consumption of emulsifying agent is 2~4 parts.
8. according to the described preparation method of claim 1, it is characterized in that in the step 3, heated and stirred 1~4 hour, stir speed (S.S.) are 300~1500 rev/mins, Heating temperature is 55~80 ℃.
9. preparation method who contains the lubrication oil anti-wear extreme pressure additive of nanoparticle comprises:
1) metal-salt or acid solution are mixed with lubricating oil dispersant, emulsifying agent and lubricant base, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain the microemulsion of salt or acid to the microemulsion clear; Said metal-salt or acid are water-soluble zirconates, water-soluble aluminum salt, boric acid or their mixture; Weight in metal-salt or acid solution is 1 part, and the consumption of base oil is 10~40 parts, and the consumption of lubricating oil dispersant is 1~6 part, and the consumption of emulsifying agent is 1~6 part;
2) will with the salt in the above-mentioned microemulsion or the alkali of sour equivalent, the speed of dividing with 0.001~0.02mol/ joins in the above-mentioned microemulsion, in temperature is 20 ℃~100 ℃, and stir speed (S.S.) is to stir 0.5~8 hour under 100~2000 rev/mins the condition, obtains final product; Said alkali is C2~C16 alkylamine or polyamines polyene, or concentration is the aqueous solution of the mineral alkali of 1~30 weight %, or ammonia;
10. according to the described preparation method of claim 9, it is characterized in that said metal-salt or acid are selected from zirconium tetrachloride, tri-chlorination zirconium, aluminum chloride, aluminum nitrate, boric acid.
11., it is characterized in that said metal-salt or aqueous acid concentration are 5~20 weight % according to the described preparation method of claim 9.
12. according to the described preparation method of claim 9, it is characterized in that, said alkali is ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine, diethylenetriamine, triethylene tetramine, tetraethylene pentamine, or concentration is the aqueous solution of 8~25% sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia, or ammonia.
13. according to the described preparation method of claim 9, it is characterized in that, said lubricating oil dispersant is allyl butyrate imide, petroleum sodium sulfonate, calcium mahogany sulfonate or their mixture, said emulsifying agent is, sorbitol monooleate, Tween-20, polyoxyethylene sorbitan monoleate or their mixture, and said dispersion aids is Pentyl alcohol, n-hexyl alcohol, n-dodecanol or their mixture.
14., it is characterized in that in the step 1, the consumption of base oil is 20~30 parts according to the described preparation method of claim 9, the consumption of lubricating oil dispersant is 2~4 parts, the consumption of emulsifying agent is 2~4 parts.
15., it is characterized in that, in the step 2 according to the described preparation method of claim 9, the speed that alkali is divided with 0.005~0.015mol/ feeds or is added dropwise in the microemulsion of salt or acid, stir speed (S.S.) is 300~1500 rev/mins, and heated and stirred 1~4 hour, Heating temperature are 55~80 ℃.
16. a preparation method who contains the lubrication oil anti-wear extreme pressure additive of nanoparticle comprises:
1) alkali is mixed with dispersion agent, emulsifying agent and lubricant base, stir, be heated to 30 ℃~120 ℃, drip dispersion aids, obtain alkaline microemulsion to the microemulsion clear; Said alkali is C2~C16 alkylamine or polyamines polyene, or concentration is the aqueous solution of the mineral alkali of 1~30 weight %; Weight in alkali or alkali lye is 1 part, and the consumption of base oil is 10~40 parts, and the consumption of lubricating oil dispersant is 1~6 part, and the consumption of emulsifying agent is 1~6 part;
2) will with the metal-salt or the acid solution of alkali equivalent in the above-mentioned microemulsion, be added dropwise in the above-mentioned microemulsion with 10~60 droplets/minute speed, in temperature is 25 ℃~100 ℃, and stir speed (S.S.) is to stir 0.5~8 hour under 100~2000 rev/mins the condition, obtains final product; Said metal-salt or acid are water-soluble zirconates, water-soluble aluminum salt, boric acid or their mixture.
17. according to the described preparation method of claim 16, it is characterized in that, said alkali is ethylamine, di-n-butyl amine, n-hexyl amine, dodecyl amine, diethylenetriamine, triethylene tetramine, tetraethylene pentamine, or concentration is the aqueous solution of 8~25% sodium hydroxide, potassium hydroxide, lithium hydroxide, water glass, ammonia.
18., it is characterized in that said metal-salt or acid are selected from zirconium tetrachloride, tri-chlorination zirconium, aluminum chloride, aluminum nitrate, boric acid according to the described preparation method of claim 16.
19., it is characterized in that the concentration of said metal-salt or aqueous acid is 5~20 weight % according to the described preparation method of claim 16.
20. according to the described preparation method of claim 16, it is characterized in that, said lubricating oil dispersant is allyl butyrate imide, petroleum sodium sulfonate, calcium mahogany sulfonate or their mixture, said emulsifying agent is, sorbitol monooleate, Tween-20, polyoxyethylene sorbitan monoleate or their mixture, and said dispersion aids is Pentyl alcohol, n-hexyl alcohol, n-dodecanol or their mixture.
21., it is characterized in that according to the described preparation method of claim 16, in the step 1, be 1 part in the weight of alkali or alkali lye, the consumption of base oil is 20~30 parts, and the consumption of lubricating oil dispersant is 2~4 parts, and the consumption of emulsifying agent is 2~4 parts.
22. according to the described preparation method of claim 16, it is characterized in that, in the step 2, will with the metal-salt or the acid solution of alkali equivalent in the alkaline microemulsion, be added dropwise in the alkaline microemulsion with 20~40 droplets/minute speed, heated and stirred 1~4 hour, stir speed (S.S.) are 300~1500 rev/mins, 55~80 ℃ of Heating temperatures.
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CN102041140A (en) * 2010-01-19 2011-05-04 无锡惠源包装有限公司 Anti-micro pitting gear oil composite additive
CN101462914B (en) * 2009-01-12 2011-12-07 山西建烨工贸有限公司 Environment protective emulsive explosive composite emulsifying agent
CN102925251A (en) * 2012-11-27 2013-02-13 沈阳工业大学 Method for preparing nano-borate particles in liquid-state lubricating oil
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CN101462914B (en) * 2009-01-12 2011-12-07 山西建烨工贸有限公司 Environment protective emulsive explosive composite emulsifying agent
CN102041140A (en) * 2010-01-19 2011-05-04 无锡惠源包装有限公司 Anti-micro pitting gear oil composite additive
CN102041140B (en) * 2010-01-19 2013-04-24 江苏惠源石油科技有限公司 Anti-micro pitting gear oil composite additive
CN101974361A (en) * 2010-08-20 2011-02-16 泰安天健应用技术推广中心 Multifunctional nanocomposite antiwear agent
CN102925251A (en) * 2012-11-27 2013-02-13 沈阳工业大学 Method for preparing nano-borate particles in liquid-state lubricating oil
CN115383534A (en) * 2022-09-13 2022-11-25 成都青洋电子材料有限公司 Production process of monocrystalline silicon wafer

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