CN1089747C - Process for prepared boronized high-basicity magnesium alkylsalicylate as additive of lubricating oil - Google Patents

Process for prepared boronized high-basicity magnesium alkylsalicylate as additive of lubricating oil Download PDF

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CN1089747C
CN1089747C CN99100369A CN99100369A CN1089747C CN 1089747 C CN1089747 C CN 1089747C CN 99100369 A CN99100369 A CN 99100369A CN 99100369 A CN99100369 A CN 99100369A CN 1089747 C CN1089747 C CN 1089747C
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reaction
warming
methyl alcohol
add
additive
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CN1262266A (en
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徐小红
付兴国
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LANZHOU OIL REFINING CHEMICAL GENERNAL PLANT CHINESE PETRO-CHEMICAL CORP
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LANZHOU OIL REFINING CHEMICAL GENERNAL PLANT CHINESE PETRO-CHEMICAL CORP
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Abstract

The present invention relates to a method for preparing boronized high-basicity magnesium alkylsalicylate as additive of lubricating oil, which is synthesized in a two-step method of preparing and boronizing high-basicity magnesium alkylsalicylate.

Description

A kind of preparation method of high-basicity magnesium alkylaslicylate as lubricant additive of boronation
The present invention relates to a kind of high-basicity magnesium alkylaslicylate as lubricant additive of boronation, belong to the lubricating oil field.
The mistakes basicity component of tradition purification agent is that the form with carbonate exists, thereby the mistakes basicity metal detergent of this carbonating can quicken the oxidation of oil under exacting terms the metallic surface appearance is worn and torn.The beginning of the nineties at the end of the eighties, external each major oil companies develop and have developed with the boride metal purification agent of borate as the alkali storehouse, as U.S.4,965,004,3,4830,548 etc., domestic also do not have a relevant patent report, and this novel boride metal purification agent not only has the effect of purification agent, and good oxidative stability arranged, excellent friction resistant polishing machine etc.
Patent 4,965,004 has described a kind of preparation method of metal detergent of boronation.It is in the presence of a kind of proton type solvent and a kind of hydrocarbon cosolvent, and boronation reagent is joined in a kind of high alkaline metal detergent, stirs, and reacts 0.25-5.0 hour, and steaming desolventizes, and after the filtration, obtains a kind of metal detergent of boronation.
Patent 3,480,548 it be with a kind of high base number metal detergent (150-175 ℃) and boric acid or other boronation reagent react under very high temperature, it carries out in the presence of the solvent not having.This just causes CO 2Overflow fast, cause serious bubble-related issues.
The process of boronation of the present invention is (30-70 ℃) that carries out under lower temperature, and begins to prepare from untreated high base number magnesium alkylsalicylate, and the boron amount is improved.
The present invention seeks to provide a kind of high-basicity magnesium alkylaslicylate as lubricant additive of boronation, thereby a kind of new additive agent of excellent property is provided for top-grade lubricating oil.
Boronation high-basicity magnesium alkylaslicylate as lubricant additive of the present invention prepares with following method: 1, the preparation of high base number magnesium alkylsalicylate.The preparation method of high base number magnesium alkylsalicylate is existing narration in patent ZL94101431.2 and ZL94101432.0.2, the methyl alcohol and the solvent that in the reaction mixture of the first step, add metering, stirring is warming up between 30~70 ℃, adds the boric acid of metering, reacts 0.5~4 hour, reaction is warming up to 110 ℃ after finishing, steaming engaging benzenemethanol and water, solubilizing agent dilution, the cooling back is centrifugal, steams desolventizing at last, gets product.
A kind of preparation method of high-basicity magnesium alkylaslicylate as lubricant additive of boronation, it is characterized in that: reactions steps is carried out in two steps: the reaction of the first step high basicity, solvent and methyl alcohol are put into reactor, stirring also is warming up to 30~60 ℃, drop into light magnesium oxide, add entry and ammoniacal liquor simultaneously, continue to stir, kept 10-13 minute, add alkyl salicylate then, and keep temperature of reaction between 30~60 ℃, carry out neutralization reaction 1 hour, and fed carbonic acid gas then and carry out high basicity reaction 2 hours, be warming up to 110 ℃, steaming engaging benzenemethanol and water, cooling.The boronation reaction of second step, the boronation temperature of reaction maintains between 30~70 ℃, and the boronation reaction times is 0.5~4 hour, and reaction is warming up to 110 ℃ after finishing, steaming engaging benzenemethanol and water, the solubilizing agent dilution, the cooling back is centrifugal, steams desolventizing at last and gets product.Add 5~45 parts of methyl alcohol in 100 parts of alkyl salicylates, 10~100 parts of solvents, 20~50 parts of boric acid, methyl alcohol must be purity greater than 95% chemical reagent or industrial goods, the reaction solvent for use is that dimethylbenzene or boiling range are 60~160 ℃ straight-run spirit, and the boric acid of reaction usefulness can be that SILVER REAGENT also can be a technical grade product.
Embodiment 1
Add 200 milliliters in gasoline in having 500 milliliters of there-necked flasks of electric mixer and condensation water trap, 90 milliliters of methyl alcohol stir, and are warming up to about 50 ℃; Drop into 16.0 gram light magnesium oxides, stir, water and ammonia water mixture (3~4 parts of water add 1 part of ammoniacal liquor) are added in the mixture for about 65 milliliters, react after 20~30 minutes, mixture becomes pasty state, adds 100.0 gram alkyl salicylates, stirs, control reaction temperature is 50~55 ℃, reacts 1 hour.After reaction is finished, feed carbonic acid gas, Ventilation Rate is 200~250 ml/min, about 120 minutes; Reaction is warming up to 110 ℃ after finishing, steaming engaging benzenemethanol and water, and 14 milliliters of methyl alcohol are added in cooling, stir, and are warming up to 50~55 ℃ then, add boric acid 24.7 grams, react about 90 minutes, carry out the boronation reaction.Reaction is warming up to 110 ℃, steaming engaging benzenemethanol and water after finishing; Cooling, the gasoline that adds twice dilutes.Reaction product under 3600 rev/mins of rotating speeds centrifugal 30 minutes removes solvent under reduced pressure after removing slag and gets product.Product Mg:5.43m%, B:1.67m%, TBN:249mgKOH/g.
Comparative example 1
Add 81 milliliters in gasoline in having 1000 milliliters of there-necked flasks of electric mixer and condensation water trap, 14 milliliters of methyl alcohol stir, and are warming up to 64 ℃; (TBN=281mgKOH/g Mg=6.45m%), and adds 16.6 gram boric acid to the magnesium alkylsalicylate of input 100.0 gram high base numbers, reacts 1.5 hours.Reaction is warming up to 110 ℃, steaming engaging benzenemethanol and water after finishing; Cooling, the gasoline that adds twice dilutes, and is centrifugal, removes solvent under reduced pressure and get product.Product Mg:5.41m%, B:0.62m%, TBN:244mgKOH/g.
Embodiment 2
Add 400 milliliters in gasoline in having 1000 milliliters of there-necked flasks of electric mixer and condensation water trap, 180 milliliters of methyl alcohol stir, and are warming up to 50~60 ℃; Drop into 32.0 gram light magnesium oxides, stir, water and ammonia water mixture are added in the mixture for about 130 milliliters, react after 20~30 minutes, add 200 gram alkyl salicylates, keeping temperature of reaction is 50~55 ℃, reacts 1 hour; Feed carbonic acid gas then, Ventilation Rate is 400~450 milliliters, is warming up to 50~60 ℃ then; Add boric acid 49.4 grams, reacted about 90 minutes, carry out boronation and react, reaction is warming up to 110 ℃ after finishing, steaming engaging benzenemethanol and water, and cooling, the gasoline that adds twice dilutes, and is centrifugal, removes solvent under reduced pressure and get product.Product Mg:5.81m%, B:3.2m%, TBN:313mgKOH/g.

Claims (2)

1, a kind of preparation method of high-basicity magnesium alkylaslicylate as lubricant additive of boronation is characterized in that this additive prepares by the following method:
Solvent and methyl alcohol are put into reactor, stir and be warming up to 30~60 ℃, drop into light magnesium oxide, add entry and ammoniacal liquor simultaneously, continue to stir, kept 10-13 minute, add alkyl salicylate then, and keep temperature of reaction between 30~60 ℃, carried out neutralization reaction 1 hour, feed carbonic acid gas then and carry out high basicity reaction 2 hours, be warming up to 110 ℃, steaming engaging benzenemethanol and water, cooling, add solvent and methyl alcohol, be warming up between 30~70 ℃, add boric acid, reacted 0.5~4 hour, reaction is warming up to 110 ℃, steaming engaging benzenemethanol and water after finishing, the solubilizing agent dilution, the cooling back is centrifugal, steams desolventizing at last and gets product, in the boronation reaction, per 100 parts of alkyl salicylates are added 5~45 parts of methyl alcohol, 10~100 parts of solvents, 20~50 parts of boric acid, reaction is that dimethylbenzene or boiling range are 60~160 ℃ straight-run spirit with solvent.
2, the preparation method of additive according to claim 1 is characterized in that: methyl alcohol must be purity greater than 95% chemical reagent or industrial goods.
CN99100369A 1999-01-26 1999-01-26 Process for prepared boronized high-basicity magnesium alkylsalicylate as additive of lubricating oil Expired - Fee Related CN1089747C (en)

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Publication number Priority date Publication date Assignee Title
CN110295079A (en) * 2019-07-19 2019-10-01 中国科学院兰州化学物理研究所 A kind of preparation and application of low-temperature lubrication oil additive
CN113234517A (en) * 2021-05-07 2021-08-10 新乡市瑞丰新材料股份有限公司 Preparation method of nano-grade high-boron-content composite magnesium detergent

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4965004A (en) * 1989-04-21 1990-10-23 Texaco Inc. Process for a borated detergent additive
CN1107461A (en) * 1994-02-23 1995-08-30 中国石化兰州炼油化工总厂 Process for preparing high-basicity magnesium alkylsalicylate

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4965004A (en) * 1989-04-21 1990-10-23 Texaco Inc. Process for a borated detergent additive
CN1107461A (en) * 1994-02-23 1995-08-30 中国石化兰州炼油化工总厂 Process for preparing high-basicity magnesium alkylsalicylate

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