CN108795538B - Fluoro-polyester type detergent, preparation method and lubricating oil composition prepared from fluoro-polyester type detergent - Google Patents

Fluoro-polyester type detergent, preparation method and lubricating oil composition prepared from fluoro-polyester type detergent Download PDF

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CN108795538B
CN108795538B CN201810752088.0A CN201810752088A CN108795538B CN 108795538 B CN108795538 B CN 108795538B CN 201810752088 A CN201810752088 A CN 201810752088A CN 108795538 B CN108795538 B CN 108795538B
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polyester
detergent
acid
lubricating oil
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CN108795538A (en
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王永垒
李海云
邢楠楠
张雅文
魏文静
张程程
王景
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Shenyang Hualun Lubricating Oil Additive Co ltd
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Huangshan University
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M161/00Lubricating compositions characterised by the additive being a mixture of a macromolecular compound and a non-macromolecular compound, each of these compounds being essential
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/682Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens
    • C08G63/6824Polyesters containing atoms other than carbon, hydrogen and oxygen containing halogens derived from polycarboxylic acids and polyhydroxy compounds
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • C08G63/82Preparation processes characterised by the catalyst used
    • C08G63/85Germanium, tin, lead, arsenic, antimony, bismuth, titanium, zirconium, hafnium, vanadium, niobium, tantalum, or compounds thereof
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
    • C10M2201/06Metal compounds
    • C10M2201/062Oxides; Hydroxides; Carbonates or bicarbonates
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/06Well-defined aromatic compounds
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/02Hydroxy compounds
    • C10M2207/021Hydroxy compounds having hydroxy groups bound to acyclic or cycloaliphatic carbon atoms
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/283Esters of polyhydroxy compounds
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/284Esters of aromatic monocarboxylic acids
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2213/00Organic macromolecular compounds containing halogen as ingredients in lubricant compositions
    • C10M2213/06Perfluoro polymers
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/044Sulfonic acids, Derivatives thereof, e.g. neutral salts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/04Detergent property or dispersant property
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/06Oiliness; Film-strength; Anti-wear; Resistance to extreme pressure
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/08Resistance to extreme temperature
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/10Inhibition of oxidation, e.g. anti-oxidants

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Lubricants (AREA)

Abstract

The invention belongs to the technical field of synthesis of lubricating oil detergents, and particularly relates to a fluoro-polyester detergent, and further discloses a preparation method thereof and a lubricating oil composition prepared from the fluoro-polyester detergent. The fluorinated polyester type detergent adopts fluorinated compounds as main organic raw materials, so that the high temperature resistance and the carbon deposition resistance of a final product are ensured; meanwhile, the polyester has larger molecular weight, more carboxyl groups and strong dispersing capacity, so that a detergent product with high base number (380-420mgKOH/g), low pour point, excellent high-temperature resistance and more stable performance can be obtained, and the fluoro-polycarboxy polyester salt with larger molecular weight can better form an adsorption film on the metal surface of an engine, thereby providing excellent high-temperature cleaning performance and greatly improving the comprehensive application performance.

Description

Fluoro-polyester type detergent, preparation method and lubricating oil composition prepared from fluoro-polyester type detergent
Technical Field
The invention belongs to the technical field of synthesis of lubricating oil detergents, and particularly relates to a fluoro-polyester detergent, and further discloses a preparation method thereof and a lubricating oil composition prepared from the fluoro-polyester detergent.
Background
The lubricating oil is a liquid or semisolid lubricating agent used on various types of automobiles and mechanical equipment to reduce friction and protect machines and workpieces, and mainly plays roles in lubrication, cooling, rust prevention, cleaning, sealing, buffering and the like. However, in the use process of the engine lubricating oil, due to harsh working conditions and high-temperature oxidation, and the absorption of acid gases of nitrogen oxides and sulfur dioxide from the outside, the lubricating oil is prone to oxidative degradation, and a certain amount of acid corrosive substances, such as sulfuric acid, nitric acid, acid sludge and the like, are generated, so that the lubricating effect of the lubricating oil is reduced and the corrosion to equipment is aggravated. Therefore, it is necessary to add a lubricating oil detergent to continuously neutralize acidic substances generated during the use of the lubricating oil and prevent the acidic substances from corroding the engine, so that the purposes of prolonging the service life of the lubricating oil and protecting the engine are achieved.
The traditional lubricating oil detergent basically uses common carbon chain small molecular organic acid, such as dodecyl benzene sulfonic acid, alkyl salicylic acid, oleic acid and the like as raw materials, alkaline components are dispersed in diluent oil through reaction, and the adopted diluent oil is mainly common mineral oil lubricating oil base oil, such as 150SN, 250SN, 350SN and other types of mineral oil. On one hand, the mineral base oils belong to products of petroleum refining, have poor degradation capability, contain certain wax, and are not suitable for the high-end lubricating oil field with high requirements on environmental protection and pour point; on the other hand, the linear organic acid raw materials selected have poor dispersion performance due to small molecules and single carboxyl contained in the linear organic acid raw materials, the base number of the prepared detergent product is about 300mgKOH/g, and the detergent product with the required high base number (380-420mgKOH/g) cannot be stably obtained; moreover, the adopted organic acid raw material is in a straight chain structure, so that the dispersing performance of alkaline components such as colloidal calcium carbonate and magnesium carbonate is unstable, colloidal carbonate is easy to precipitate under the working condition of high-temperature use, and the cleaning dispersing capacity of the colloidal carbonate is reduced; moreover, because the molecules of the formed organic acid salt are too small, a stable adsorption film cannot be formed on the surface of the metal, and the detergency and protection capability of the engine are insufficient; especially, organic acid and diluent oil in the raw materials are compounds with common carbon chains, and the compounds have poor high temperature resistance, are easy to degrade under the action of high temperature, are easy to generate carbon deposition and influence the service performance of the compounds. Therefore, the development of new detergent products has been imperative.
Disclosure of Invention
Therefore, the technical problem to be solved by the invention is to provide a fluoro polyester type detergent, and further disclose a preparation method thereof and a lubricating oil composition prepared by the same.
In order to solve the technical problems, the fluoro polyester detergent provided by the invention is prepared from the following raw materials in molar weight:
Figure BDA0001725806770000021
preferably, the fluoro polyester type detergent is prepared by raw materials comprising the following raw material components in molar quantity:
Figure BDA0001725806770000031
the fluoro-polycarboxyl polyester resin is prepared by taking tetrafluorosuccinic acid, tetrafluorobutanediol, 3-fluoro-1, 2-propanediol and citric acid as raw materials and carrying out polymerization reaction at 220 ℃ in the presence of a catalyst.
The molar ratio of tetrafluorosuccinic acid, tetrafluorobutanediol, 3-fluoro-1, 2-propanediol and citric acid is 0.2-0.8: 0.5-1.5: 0.2-0.8: 1-2, and preferably 0.5: 1: 0.5: 1.5; the catalyst is preferably dibutyltin oxide, and the addition amount accounts for 0.5 wt% of the total amount of the materials.
The 12-phenylbutyryl stearic acid is prepared by taking phenylbutyric acid and 12-hydroxystearic acid as raw materials, and reacting the raw materials at the temperature of 120-160 ℃ by taking dimethylbenzene as a water-carrying agent under the catalytic action.
The molar ratio of the phenylbutyric acid to the 12-hydroxystearic acid is preferably 1: preferably, the catalyst is tetrabutyl titanate.
The dispersion stabilizer comprises triglycerol monostearate;
the solvent comprises toluene or xylene;
the promoter comprises trimethylamine or methanol.
The invention also discloses a method for preparing the fluoro polyester type detergent, which comprises the following steps:
(1) according to the selected molar weight, fully mixing the fluorinated polycarboxy polyester, 12-phenylbutyryl stearic acid, perfluorooctane sulfonic acid, pentaerythritol tetra-n-heptanoate, calcium hydroxide, active magnesium oxide, a solvent, an accelerant and a dispersion stabilizer, and carrying out neutralization reaction at 35-60 ℃;
(2) and then adding water with a selected molar weight, heating the reaction system to 65-80 ℃, introducing carbon dioxide gas with a selected molar weight for reaction, removing residues from the reaction product, and distilling under reduced pressure to remove the solvent to obtain the catalyst.
The aeration rate of the carbon dioxide gas is 60-300 mL/min.
The invention also discloses a lubricating oil composition which comprises the fluoro polyester type detergent.
Specifically, the addition amount of the fluoro polyester type detergent is 1-3% of the mass of the base oil.
The base oil includes synthetic ester base oils such as pentaerythritol tetraheptanoate, trimethylolpropane triheptanoate, and the like.
According to the fluorinated polyester type detergent, fluorinated carboxyl polyester resin with a large molecular weight is used as a main carboxyl raw material, organic acid 12-phenylbutyryl stearic acid with a phenyl branched chain and better compatibility with base oil and a proper amount of perfluorooctane sulfonate are matched as main organic acid raw materials, pentaerythritol tetra-n-heptanoate with good solubility on the fluorinated carboxyl polyester resin is used as base oil, and calcium hydroxide and magnesium oxide are used as basic raw materials, so that the polyester type detergent mixed with calcium and magnesium salts is obtained. The main organic raw materials of the polyester detergent adopt fluoro compounds, so that the high temperature resistance and the carbon deposition resistance of a final product are ensured; meanwhile, the polyester has larger molecular weight, more carboxyl groups and strong dispersing capacity, so that a detergent product with high base number (380-420mgKOH/g), low pour point, excellent high-temperature resistance and more stable performance can be obtained, and the fluoro-polycarboxy polyester salt with larger molecular weight can better form an adsorption film on the metal surface of an engine, thereby providing excellent high-temperature cleaning performance. Compared with the main detergent products of the conventional common carbon chain structure diluent oil such as 150SN base oil, 250SN base oil, 350SN base oil and the like in the market, the detergent has better self oxidation resistance, reduced pour point, improved high temperature resistance, obviously improved precipitation condition of colloid, can be used in areas with the temperature lower than minus 30 ℃, and greatly improved comprehensive application performance.
Detailed Description
EXAMPLE 1 Synthesis of Fluoropolycarboxy polyester resin
According to a molar ratio of 0.5: 1: 0.5: 1.5 adding tetrafluorosuccinic acid, tetrafluorobutanediol, 3-fluoro-1, 2-propanediol and citric acid into a reactor, adding dibutyltin oxide accounting for 0.5 wt% of the total amount of the materials as a catalyst, and heating the reaction system to 180-220 ℃ for carrying out polymerization reaction for 8-12h to obtain the fluorocarboxyl polyester resin. The acid value of the obtained polyester resin is detected to be 200-240 mgKOH/g.
Example 212 Synthesis of phenylbutyryl stearic acid
According to a molar ratio of 1: 1, adding phenylbutyric acid and 12-hydroxystearic acid into a reactor, adding dimethylbenzene serving as a water-carrying agent under the catalytic action of tetrabutyl titanate, reacting at the temperature of 120-160 ℃ for 2-6h, and removing a dimethylbenzene solvent under reduced pressure after the reaction is finished to obtain the 12-phenylbutyryl stearic acid.
The specific synthetic process and molecular structure are as follows:
Figure BDA0001725806770000051
example 3
The fluoro polyester type detergent is prepared by the following raw material components in molar quantity:
Figure BDA0001725806770000052
Figure BDA0001725806770000061
the preparation method of the fluoro polyester detergent comprises the following steps:
(1) according to the selected molar weight, fully mixing the fluorinated polycarboxy polyester, 12-phenylbutyryl stearic acid, perfluorooctane sulfonic acid, pentaerythritol tetra-n-heptanoate, calcium hydroxide, active magnesium oxide, a solvent, an accelerator and a dispersion stabilizer, and carrying out neutralization reaction at 35 ℃;
(2) and then adding a selected amount of water, heating the reaction system to 65 ℃, introducing carbon dioxide gas with a selected molar amount at an aeration rate of 60mL/min for reaction, removing residues from the reaction product, and distilling under reduced pressure to remove the solvent to obtain light yellow transparent liquid.
Example 4
The fluoro polyester type detergent is prepared by the following raw material components in molar quantity:
Figure BDA0001725806770000062
Figure BDA0001725806770000071
the preparation method of the fluoro polyester detergent comprises the following steps:
(1) according to the selected molar weight, fully mixing the fluorinated polycarboxy polyester, 12-phenylbutyryl stearic acid, perfluorooctane sulfonic acid, pentaerythritol tetra-n-heptanoate, calcium hydroxide, active magnesium oxide, a solvent, an accelerator and a dispersion stabilizer, and carrying out neutralization reaction at 60 ℃;
(2) and then adding water with a selected molar weight, heating the reaction system to 80 ℃, introducing a selected amount of carbon dioxide gas at the aeration rate of 300mL/min for reaction, removing residues from the reaction product, and distilling under reduced pressure to remove the solvent to obtain light yellow transparent liquid.
Example 5
The fluoro polyester type detergent is prepared by the following raw material components in molar quantity:
Figure BDA0001725806770000072
the preparation method of the fluoro polyester detergent comprises the following steps:
(1) according to the selected molar weight, fully mixing the fluorinated polycarboxy polyester, 12-phenylbutyryl stearic acid, perfluorooctane sulfonic acid, pentaerythritol tetra-n-heptanoate, calcium hydroxide, active magnesium oxide, a solvent, an accelerator and a dispersion stabilizer, and carrying out neutralization reaction at 45 ℃;
(2) and then adding water with a selected molar weight, heating the reaction system to 70 ℃, introducing a selected amount of carbon dioxide gas at the ventilation rate of 180mL/min for reaction, removing residues from the reaction product, and distilling under reduced pressure to remove the solvent to obtain light yellow transparent liquid.
Example 6
The fluoro polyester type detergent is prepared by the following raw material components in molar quantity:
Figure BDA0001725806770000081
the fluorinated polyester detergent described in this example was prepared in the same manner as in example 5.
Example 7
The fluoro polyester type detergent is prepared by the following raw material components in molar quantity:
Figure BDA0001725806770000091
the fluorinated polyester detergent described in this example was prepared in the same manner as in example 5.
Comparative example 1
The starting components of the fluoro-polyester detergent described in this example were the same as in example 5 except that the fluoro-polycarboxy polyester resin was not included.
Comparative example 2
The starting components of the fluoro-polyester type detergent described in this example were the same as in example 5 except that the fluoro-polycarboxy polyester resin was changed to a commercially available ordinary polyester resin, type: YL9050A, Industrial products, Huangshan Yongli New Material science and technology Co., Ltd.
Comparative example 3
The starting components of the fluoro polyester detergent described in this example were the same as in example 5 except that 12-phenylbutyryl stearic acid was simply replaced with commercially available stearic acid.
Comparative example 4
The base composition of the fluoro polyester detergent described in this example was the same as in example 5 except that perfluorooctanesulfonic acid was not contained.
Comparative example 5
The starting components of the fluoro polyester detergent described in this example were the same as in example 5 except that only perfluorooctane sulfonic acid was replaced with commercially available dodecylbenzene sulfonic acid.
Comparative example 6
The starting components of the fluoro-polyester type detergent described in this example were the same as those of example 5 except that only the pentaerythritol tetra-n-heptanoate base oil was replaced with a common commercially available diluent oil (150SN base oil) which was purchased from oil products, Inc. of Saussuren Seisakusho.
Comparative example 7
The starting components of the fluoro-polyester detergent described in this example were the same as in example 5 except that only the pentaerythritol tetra-n-heptanoate base oil was replaced with a common commercially available diluent oil (250SN base oil) which was purchased from oil products, Inc. of Saussuren Seisattva.
Comparative example 8
The starting components of the fluoro-polyester type detergent described in this example were the same as those of example 5 except that only the pentaerythritol tetra-n-heptanoate base oil was replaced with a common commercially available diluent oil (350SN base oil) which was purchased from oil products, Inc. of Saussuren Seisakusho.
Examples of the experiments
The detergents prepared in the above examples 3 to 7 and comparative examples 1 to 8 were tested for their properties, and the test indexes included base number, viscosity, thermal stability, colloidal precipitation and pour point. Wherein, the base number is determined according to SH/T0251-1993 petroleum product base number determination method (perchloric acid potentiometry titration method); the viscosity measurement is based on GB/T265-88 petroleum product kinematic viscosity measurement method and dynamic viscometer algorithm; thermal stability and colloidal precipitation are determined by SH/T0300-92 crankcase simulation test method (QZX method); the pour point is determined according to GB/T3535-. Specific assay data are shown in table 1 below.
TABLE 1 detergent product data
Figure BDA0001725806770000111
As can be seen from the data in the table, in the detergent of the invention, the product of the polyester mixed calcium and magnesium salt detergent with high base number (380-420mgKOH/g), low pour point and excellent high temperature resistance is prepared by using the fluoro-polycarboxy polyester resin, matching with the branched 12-phenylbutyryl stearic acid and perfluorooctane sulfonic acid as the raw materials of the organic acid, and using pentaerythritol tetra-n-heptanoate as the base oil; compared with main detergent products of conventional common carbon chain structure diluent oil such as 150SN base oil, 250SN base oil, 350SN base oil and the like in the market, the detergent has better oxidation resistance, lower pour point, higher high-temperature resistance and obviously improved precipitation condition of colloid, can be used in areas with the temperature lower than minus 30 ℃, and has greatly improved application performance.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications therefrom are within the scope of the invention.

Claims (9)

1. The fluoro polyester type detergent is characterized in that the preparation raw materials comprise the following raw material components in molar quantity:
Figure FDA0002889693280000011
the fluoro-polycarboxyl polyester resin is prepared by taking tetrafluorosuccinic acid, tetrafluorobutanediol, 3-fluoro-1, 2-propanediol and citric acid as raw materials and carrying out polymerization reaction at 220 ℃ in the presence of a catalyst.
2. A fluoro-polyester detergent as claimed in claim 1, characterised in that its raw materials for preparation comprise the following raw components in molar amounts:
Figure FDA0002889693280000012
Figure FDA0002889693280000021
3. the fluoro-polyester detergent as claimed in claim 1 or 2, wherein the 12-phenylbutyryl stearic acid is prepared by using phenylbutyric acid and 12-hydroxystearic acid as raw materials, and xylene as a water-carrying agent under the catalysis, and reacting at the temperature of 120-160 ℃.
4. A fluoro polyester detergent as claimed in claim 3, characterised in that:
the dispersion stabilizer comprises triglycerol monostearate;
the solvent comprises toluene or xylene;
the promoter comprises trimethylamine or methanol.
5. A method of making a fluoro-polyester detergent as claimed in any one of claims 1 to 4, comprising the steps of:
(1) according to the selected molar weight, fully mixing the fluorinated polycarboxy polyester, 12-phenylbutyryl stearic acid, perfluorooctane sulfonic acid, pentaerythritol tetra-n-heptanoate, calcium hydroxide, active magnesium oxide, a solvent, an accelerant and a dispersion stabilizer, and carrying out neutralization reaction at 35-60 ℃;
(2) and then adding water with a selected molar weight, heating the reaction system to 65-80 ℃, introducing carbon dioxide gas with a selected molar weight for reaction, removing residues from the reaction product, and distilling under reduced pressure to remove the solvent to obtain the catalyst.
6. The method of manufacturing the fluoro polyester detergent as claimed in claim 5, wherein the aeration rate of the carbon dioxide gas is 60 to 300 mL/min.
7. A lubricating oil composition comprising the fluoro polyester type detergent as claimed in any one of claims 1 to 4.
8. Lubricating oil composition according to claim 7, characterized in that the fluoro-polyester detergent is added in an amount of 1 to 3% by mass of the base oil.
9. The lubricating oil composition of claim 8, wherein the base oil comprises a synthetic ester base oil.
CN201810752088.0A 2018-07-10 2018-07-10 Fluoro-polyester type detergent, preparation method and lubricating oil composition prepared from fluoro-polyester type detergent Active CN108795538B (en)

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