CN115368960A - Metal cutting fluid and application thereof - Google Patents

Metal cutting fluid and application thereof Download PDF

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CN115368960A
CN115368960A CN202211033287.9A CN202211033287A CN115368960A CN 115368960 A CN115368960 A CN 115368960A CN 202211033287 A CN202211033287 A CN 202211033287A CN 115368960 A CN115368960 A CN 115368960A
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ether
phosphate
cutting fluid
metal cutting
alcohol polyoxyethylene
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钟航
王秋英
王学元
高宏飞
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Jiangsu Zhongshan New Material Co ltd
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    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
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    • C10M2201/00Inorganic compounds or elements as ingredients in lubricant compositions
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    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
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    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/10Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
    • C10M2209/104Polyethers, i.e. containing di- or higher polyoxyalkylene groups of alkylene oxides containing two carbon atoms only
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    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/10Macromolecular compoundss obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/103Polyethers, i.e. containing di- or higher polyoxyalkylene groups
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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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    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
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    • C10M2215/223Five-membered rings containing nitrogen and carbon only
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    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04Phosphate esters
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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
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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
    • C10N2030/12Inhibition of corrosion, e.g. anti-rust agents or anti-corrosives
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/26Waterproofing or water resistance
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    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/28Anti-static
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10N2030/00Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
    • C10N2030/64Environmental friendly compositions
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    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/20Metal working
    • C10N2040/22Metal working with essential removal of material, e.g. cutting, grinding or drilling

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Abstract

The invention provides a metal cutting fluid and application thereof, belonging to the technical field of metal cutting fluids. The metal cutting fluid comprises the following components: 10-15 parts of phosphate, 5-7 parts of potassium carbonate, 0.02-0.07 part of ethylene diamine tetraacetic acid, 2-4 parts of C14 alcohol polyoxyethylene (3) ether, 0.2-0.7 part of benzotriazole, 0.3-0.8 part of ethylene glycol dimethyl ether, 0.2-0.7 part of ethylene glycol dimethyl ether and 60-80 parts of water; the phosphate ester comprises one or more of oleyl alcohol polyoxyethylene (3) ether phosphate, arachidyl alcohol polyoxyethylene (4) ether phosphate and stearyl alcohol polyoxyethylene (4) ether phosphate. The metal cutting fluid has the advantages of high lubricity and good antirust performance.

Description

Metal cutting fluid and application thereof
Technical Field
The invention belongs to the technical field of metal cutting fluid, and particularly relates to metal cutting fluid and application thereof.
Background
The metal cutting fluid is essential in the metal processing process and is widely applied to industries such as 3C, automobile, aerospace, machining and the like. The metal processing process can be divided into four categories of cutting, forming, protecting and heat treatment according to the treatment mode. The metal cutting fluid is widely applied to various metal cutting processing technologies, such as turning, grinding, milling and the like, and has the functions of lubrication, cooling, rust prevention, cleaning and the like in the processing process.
Currently, metal cutting fluids are mainly classified into oil-based cutting fluids and water-based cutting fluids. The oil-based cutting fluid has the advantages of great environmental pollution, flammability and slow cooling in the using process, and organic matters are needed in the cleaning process, thus causing serious harm to human bodies; compared with oil-based cutting fluid, the water-based cutting fluid has excellent cooling and cleaning performances, low cost and no pollution, but the lubricating performance and the antirust performance of the water-based cutting fluid are unsatisfactory.
Disclosure of Invention
In view of the above-mentioned drawbacks, the present invention provides a metal cutting fluid having high lubricity and excellent rust prevention properties.
The purpose of the invention is realized by adopting the following technical scheme:
a metal cutting fluid comprises the following components: 10-15 parts of phosphate, 5-7 parts of potassium carbonate, 0.02-0.07 part of ethylenediamine tetraacetic acid, 2-4 parts of C14 alcohol polyoxyethylene (3) ether, 0.2-0.7 part of benzotriazole, 0.3-0.8 part of glycol dimethyl ether, 0.2-0.7 part of glycol dimethyl ether and 60-80 parts of water;
the phosphate comprises one or more of oleyl alcohol polyoxyethylene (3) ether phosphate, arachidyl alcohol polyoxyethylene (4) ether phosphate and stearyl alcohol polyoxyethylene (4) ether phosphate.
In the invention, the phosphate is prepared by the following method: carrying out polymerization reaction on oleyl alcohol or arachidyl alcohol or octadecanol and ethylene oxide under the catalysis of potassium hydroxide to obtain polyoxyethylene ether; and carrying out esterification reaction on the polyoxyethylene ether and phosphorus pentoxide in the presence of a catalyst, and then adding water for hydrolysis to obtain the phosphate.
In the invention, the catalyst is an MCM22/ZSM-35 composite molecular sieve loaded with silicotungstic acid.
In the invention, the catalyst is prepared by adopting the following method: mixing the components in a mass ratio of 9-11:28-32:52-58:390-410:490-510 of sodium metaaluminate, sodium hydroxide, hexamethyleneimine, sodium silicate and deionized water, adding into the synthesis kettle in sequence under continuous stirring, and reacting for 45-55h at 130-150 ℃; after the reaction is finished, cooling, centrifuging, drying and roasting the precipitate to obtain the MCM22/ZSM-35 composite molecular sieve; mixing the components in a mass ratio of 10: mixing the MCM22/ZSM-35 composite molecular sieve of 3.8-5.8 with silicotungstic acid at 80-100 ℃, stirring and drying.
In the invention, the phosphate ester is a mixture of oleyl alcohol polyoxyethylene (3) ether phosphate ester and arachidyl alcohol polyoxyethylene (4) ether phosphate ester in a mass ratio of 2-4.
The invention also provides a preparation method of the metal cutting fluid, which is characterized in that water is added into phosphate, and the phosphate is stirred to obtain phosphate aqueous solution; sequentially adding potassium carbonate, ethylene diamine tetraacetic acid, C14 alcohol polyoxyethylene (3) ether, benzotriazole and ethylene glycol dimethyl ether into the phosphate aqueous solution, and uniformly stirring to obtain the metal cutting fluid.
Has the advantages that: the water-based metal cutting fluid disclosed by the invention has excellent lubricating property, wear resistance, rust resistance, hard water resistance, antistatic property, wettability and cooling effect, has wide universality on various cutting modes and workpiece materials, is non-toxic and harmless to human bodies and skin, has no pollution to the environment, and is suitable for machining various metals. The water-based metal cutting fluid is simple in production process and low in cost.
Drawings
FIG. 1 is an infrared spectrum of oleyl alcohol polyoxyethylene (3) ether phosphate B, in wavenumbers on the abscissa and in cm -1, The ordinate is the light transmission in%.
FIG. 2 NMR spectrum of oleyl alcohol polyoxyethylene (3) ether phosphate B, chemical shifts are plotted on the abscissa in ppm.
Detailed Description
Example 1
1. Preparation of oleyl alcohol polyoxyethylene (3) ether phosphate A
The method comprises the following steps: adding 268.49g of oleyl alcohol and 0.5g of potassium hydroxide into a reaction kettle, filling nitrogen to replace air in the reaction kettle, heating to 110 ℃ under a stirring state, keeping the temperature, introducing 132.15g of ethylene oxide for reaction, wherein the time for introducing the ethylene oxide is 1 hour; when the introduction of ethylene oxide is stopped, the temperature is kept at 110 ℃ for 1h for aging, then the vacuum pumping is carried out to remove impurities, and 1g of phosphoric acid is added for neutralization, thus obtaining the oleyl alcohol polyoxyethylene (3) ether.
Step two: in 400g of oleyl polyoxyethylene (3) ether, 70.8g of phosphorus pentoxide (35.4 g each time, half an hour between two times) was added in portions, and then heated to 70 ℃ and reacted at 70 ℃ for 4 hours; adding deionized water with the mass of 2 percent of the oleyl alcohol polyoxyethylene (3) ether, and hydrolyzing at 75 ℃ for 3h to obtain oleyl alcohol polyoxyethylene (3) ether phosphate A. According to QB/T2949-2008, the oleyl alcohol polyoxyethylene (3) ether phosphate A is detected to have the mass percentage of the monoester of 50.8 percent and the mass percentage of the diester of 48.6 percent.
Example 2
1. Preparation of catalyst X
A process for preparing catalyst X comprising the steps of:
the method comprises the following steps: 10g of sodium metaaluminate, 30g of sodium hydroxide, 55g of hexamethyleneimine, 400g of sodium silicate and 500g of deionized water are sequentially added into a synthesis kettle under the condition of continuous stirring. The kettle is sealed and then put into a drying oven, dynamic synthesis is carried out by adopting a mode of rotating the kettle body, the reaction temperature is set to be 140 ℃, and the reaction time is set to be 50h. After the reaction is finished, the reaction kettle is unloaded, immersed into water with the temperature of 10 ℃ for rapid cooling, and then centrifuged, and the precipitate is taken out. And drying the obtained precipitate at 110 ℃ for 10h, and then roasting at 540 ℃ for 4h to obtain the MCM22/ZSM-35 composite molecular sieve.
Step two: mixing 10g of MCM22/ZSM-35 composite molecular sieve with 4.8g of silicotungstic acid at 90 ℃, stirring for 3h, taking out, and drying in an oven at 150 ℃ for 4h to obtain the catalyst X.
2. Preparation of oleyl alcohol polyoxyethylene (3) ether phosphate B
The method comprises the following steps: adding 268.49g of oleyl alcohol and 0.5g of potassium hydroxide into a reaction kettle, filling nitrogen to replace air in the reaction kettle, heating to 110 ℃ under the stirring state, keeping the temperature, introducing 132.15g of ethylene oxide, wherein the time for introducing the ethylene oxide is 1 hour; when the introduction of ethylene oxide is stopped, preserving the heat at 110 ℃ for 1h for aging, then vacuumizing to remove impurities, and adding 1g of phosphoric acid for neutralization to obtain oleyl alcohol polyoxyethylene (3) ether;
step two: to 400g of oleyl alcohol polyoxyethylene (3) ether, 0.471g of catalyst X was added, 70.8g of phosphorus pentoxide was added in portions (35.4 g each time, two times with half an hour interval), and then the temperature was raised to 75 ℃ and reacted at 75 ℃ for 4 hours; adding deionized water with the mass of 2 percent of the oleyl alcohol polyoxyethylene (3) ether, and hydrolyzing at 75 ℃ for 3h to obtain oleyl alcohol polyoxyethylene (3) ether phosphate B. Detecting according to QB/T2949-2008, and finding that the mass percentage of the monoester is 95.6 percent and the mass percentage of the diester is 3.9 percent;
the infrared spectrum of oleyl alcohol polyoxyethylene (3) ether phosphate B is shown in FIG. 1. Wave number 3672.76cm -1 The broad peak is the characteristic peak of O-H stretching vibration, 2922.35cm -1 Is represented by-CH 3 Antisymmetric telescopic vibration absorption peak, 1063.26cm -1 And 875.12cm -1 The peak positions are respectively a P-O-C stretching vibration absorption peak and a deformation stretching vibration absorption peak of 1457.62cm -1 The absorption peak at (A) is a long carbon chain-CH 2 Thus, it was confirmed that oleyl alcohol polyoxyethylene (3) ether and P 2 O 5 Esterification reaction occurs to produce oleyl polyoxyethylene (3) ether phosphate ester B.
The NMR spectrum of oleyl alcohol polyoxyethylene (3) ether phosphate B is shown in FIG. 2. When 3.9942ppm is the absorption peak of oleyl alcohol polyoxyethylene (3) ether monoester, 0.8656ppm is the absorption peak of oleyl alcohol polyoxyethylene (3) ether diester, and 7.3696ppm is the solvent peak, it was confirmed that: oleyl polyoxyethylene (3) ether with P 2 O 5 Esterification reaction occurs to generate the mono-ester and the diester of oleyl alcohol polyoxyethylene (3) ether.
Example 3
1. Preparation of arachidyl alcohol polyoxyethylene (4) ether phosphate
The method comprises the following steps: adding 298.55g of arachidyl alcohol and 0.5g of potassium hydroxide into a reaction kettle, filling nitrogen to replace air in the reaction kettle, heating to 110 ℃ under a stirring state, preserving heat, introducing 132.15g of ethylene oxide, and introducing the ethylene oxide for 1h; when the introduction of ethylene oxide is stopped, keeping the temperature at 110 ℃ for 1h for aging, then vacuumizing to remove impurities, and adding 1g of phosphoric acid for neutralization to obtain the arachidyl alcohol polyoxyethylene (4) ether;
step two: to 430 g of arachidonoyl polyoxyethylene (4) ether, 0.478g of catalyst X (prepared by the method in example 2) was added, 48g of phosphorus pentoxide were added in portions (24 g each time, two times with half an hour interval), and the mixture was heated to 70 ℃ to react at 70 ℃ for 4 hours; adding deionized water with the mass of 3% of that of the arachidonol polyoxyethylene (4) ether, and hydrolyzing at 75 ℃ for 3h to obtain the arachidonol polyoxyethylene (4) ether phosphate. The detection is carried out according to QB/T2949-2008, and the mass percentage of the monoester and the mass percentage of the diester are respectively 96.2% and 3.22%.
Example 4
1. Preparation of Octadecanol Polyoxyethylene (4) Ether phosphate
The method comprises the following steps: adding 270.50g of octadecanol and 0.6g of potassium hydroxide into a reaction kettle, filling nitrogen to replace air in the reaction kettle, heating to 110 ℃ under the stirring state, preserving heat, introducing 176.2g of ethylene oxide, and introducing the ethylene oxide for 1 hour; when the introduction of ethylene oxide is stopped, keeping the temperature at 110 ℃ for 1h for aging, then vacuumizing to remove impurities, and adding 1.2g of phosphoric acid for neutralization to obtain octadecanol polyoxyethylene (4) ether;
step two: 446 g of octadecanol polyoxyethylene (4) ether is added with 0.480g of catalyst X, 48g of phosphorus pentoxide is added in batches (24 g of phosphorus pentoxide is added each time, half an hour is separated from each other), then the temperature is raised to 70 ℃, and the reaction is carried out for 4 hours at 70 ℃; adding deionized water with the mass of 2 percent of the octadecanol polyoxyethylene (4) ether, and hydrolyzing at 75 ℃ for 1h to obtain the octadecanol polyoxyethylene (4) ether phosphate. The detection is carried out according to QB/T2949-2008, and the mass percentage of the monoester and the mass percentage of the diester are respectively 96.2% and 3.19%.
EXAMPLE 5 preparation of Metal cutting fluid
Six aqueous solutions of phosphate were prepared separately: taking 12 parts by mass of oleyl alcohol polyoxyethylene (3) ether phosphate A prepared in example 1, adding 70 parts by mass of deionized water, and stirring for half an hour to obtain a phosphate aqueous solution A; taking 12 parts by mass of oleyl alcohol polyoxyethylene (3) ether phosphate B prepared in example 2, adding 70 parts by mass of deionized water, and stirring for half an hour to obtain a phosphate aqueous solution B; taking 12 parts by mass of the arachidyl alcohol polyoxyethylene (4) ether phosphate prepared in example 3, adding 70 parts by mass of deionized water, and stirring for half an hour to obtain a phosphate aqueous solution C; mixing 3 parts by mass of oleyl alcohol polyoxyethylene (3) ether phosphate B prepared in example 2 and 9 parts by mass of arachidyl alcohol polyoxyethylene (4) ether phosphate prepared in example 3, adding 70 parts by mass of deionized water, and stirring for half an hour to obtain a phosphate aqueous solution D; mixing 3 parts by mass of the arachidonoyl alcohol polyoxyethylene (4) ether phosphate prepared in example 3 and 9 parts by mass of the octadecanoyl alcohol polyoxyethylene (4) ether phosphate prepared in example 4, adding 70 parts by mass of deionized water, and stirring for half an hour to obtain a phosphate aqueous solution E; and adding 70 parts by mass of deionized water into 12 parts of tricresyl phosphate, and stirring for half an hour to obtain a phosphate aqueous solution F.
Respectively adopting phosphate aqueous solutions A-F to prepare metal cutting fluid, wherein the specific method comprises the following steps: sequentially adding 6 parts by mass of potassium carbonate, 0.05 part by mass of ethylene diamine tetraacetic acid, 3 parts by mass of C14 alcohol polyoxyethylene (3) ether (brand AEO3, number average molecular weight of 312-352, a new material purchased from Jiangsu Zhongshan), 0.5 part by mass of benzotriazole and 0.5 part by mass of ethylene glycol dimethyl ether into a phosphate aqueous solution, and uniformly stirring to obtain metal cutting fluids A, B, C, D, E and F.
The properties of the metal cutting fluids a to F were tested as follows: the maximum non-seizing load (PB/N) of the cutting fluid is obtained according to GB/T3142-2019 four-ball method for measuring the bearing capacity of the lubricant; performing an antirust test according to GB/T6144-2010; performing stability test according to SH/T0365-92; the degradability test was carried out according to SH/T0365-92.
TABLE 1 test results
Figure BDA0003818308280000051
As can be seen from Table 1, the cutting fluid D prepared by compounding the oleyl alcohol polyoxyethylene (3) ether phosphate with high monoester content and the arachidyl alcohol polyoxyethylene (4) ether phosphate with the special phosphate prepared by the method has greatly improved lubricating property, antirust property, biodegradation property and stability, and has good application prospect in the direction of metal cutting fluid.
The foregoing is a further detailed description of the invention in connection with specific preferred embodiments and it is not intended to limit the invention to the specific embodiments described. For those skilled in the art to which the invention pertains, several simple deductions or substitutions can be made without departing from the spirit of the invention, and all shall be considered as belonging to the protection scope of the invention.

Claims (6)

1. The metal cutting fluid is characterized by comprising the following components: 10-15 parts of phosphate, 5-7 parts of potassium carbonate, 0.02-0.07 part of ethylene diamine tetraacetic acid, 2-4 parts of C14 alcohol polyoxyethylene (3) ether, 0.2-0.7 part of benzotriazole, 0.3-0.8 part of ethylene glycol dimethyl ether, 0.2-0.7 part of ethylene glycol dimethyl ether and 60-80 parts of water;
the phosphate comprises one or more of oleyl alcohol polyoxyethylene (3) ether phosphate, arachidyl alcohol polyoxyethylene (4) ether phosphate and stearyl alcohol polyoxyethylene (4) ether phosphate.
2. The metal cutting fluid according to claim 1, wherein the phosphate ester is prepared by a method comprising: carrying out polymerization reaction on oleyl alcohol or arachidyl alcohol or octadecanol and ethylene oxide under the catalysis of potassium hydroxide to obtain polyoxyethylene ether; and carrying out esterification reaction on the polyoxyethylene ether and phosphorus pentoxide in the presence of a catalyst, and then adding water for hydrolysis to obtain the phosphate.
3. The metal cutting fluid according to claim 2, wherein the catalyst is an MCM22/ZSM-35 composite molecular sieve loaded with silicotungstic acid.
4. The metal cutting fluid according to claim 3, wherein the catalyst is prepared by the following method: mixing the components in a mass ratio of (9-11): 28-32:52-58:390-410:490-510 parts of sodium metaaluminate, sodium hydroxide, hexamethyleneimine, sodium silicate and deionized water are sequentially added into a synthesis kettle under continuous stirring, and the reaction is carried out for 45-55 hours at 130-150 ℃; after the reaction is finished, cooling, centrifuging, drying and roasting the precipitate to obtain the MCM22/ZSM-35 composite molecular sieve; mixing the components in a mass ratio of 10: mixing the MCM22/ZSM-35 composite molecular sieve of 3.8-5.8 with silicotungstic acid at 80-100 ℃, stirring and drying.
5. The metal cutting fluid according to claim 4, wherein the phosphate ester is a mixture of oleyl alcohol polyoxyethylene (3) ether phosphate ester and arachidyl alcohol polyoxyethylene (4) ether phosphate ester in a mass ratio of 2 to 4.
6. The method for producing a metal cutting fluid according to claim 1, wherein water is added to the phosphate and the mixture is stirred to obtain an aqueous phosphate solution; sequentially adding potassium carbonate, ethylene diamine tetraacetic acid, C14 alcohol polyoxyethylene (3) ether, benzotriazole and ethylene glycol dimethyl ether into the phosphate aqueous solution, and uniformly stirring to obtain the metal cutting fluid.
CN202211033287.9A 2022-08-26 2022-08-26 Metal cutting fluid and application thereof Pending CN115368960A (en)

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