CN115851355B - CNC cutting oil for copper-aluminum composite material of new energy automobile - Google Patents
CNC cutting oil for copper-aluminum composite material of new energy automobile Download PDFInfo
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- CN115851355B CN115851355B CN202211698397.7A CN202211698397A CN115851355B CN 115851355 B CN115851355 B CN 115851355B CN 202211698397 A CN202211698397 A CN 202211698397A CN 115851355 B CN115851355 B CN 115851355B
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- 239000010730 cutting oil Substances 0.000 title claims abstract description 34
- JRBRVDCKNXZZGH-UHFFFAOYSA-N alumane;copper Chemical compound [AlH3].[Cu] JRBRVDCKNXZZGH-UHFFFAOYSA-N 0.000 title claims abstract description 17
- 239000002131 composite material Substances 0.000 title claims abstract description 17
- 239000013530 defoamer Substances 0.000 claims abstract description 28
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 24
- 239000002199 base oil Substances 0.000 claims abstract description 22
- 239000002518 antifoaming agent Substances 0.000 claims abstract description 16
- 239000002994 raw material Substances 0.000 claims abstract description 13
- 238000005260 corrosion Methods 0.000 claims abstract description 10
- 230000007797 corrosion Effects 0.000 claims abstract description 10
- 239000003112 inhibitor Substances 0.000 claims abstract description 10
- 229910052751 metal Inorganic materials 0.000 claims abstract description 8
- 239000002184 metal Substances 0.000 claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 claims description 42
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 21
- 239000002253 acid Substances 0.000 claims description 18
- 229910019142 PO4 Inorganic materials 0.000 claims description 15
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 15
- 239000010452 phosphate Substances 0.000 claims description 15
- 238000003756 stirring Methods 0.000 claims description 15
- 238000002360 preparation method Methods 0.000 claims description 11
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims description 10
- 239000004721 Polyphenylene oxide Substances 0.000 claims description 10
- 229920000570 polyether Polymers 0.000 claims description 10
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 claims description 8
- HMMGMWAXVFQUOA-UHFFFAOYSA-N octamethylcyclotetrasiloxane Chemical compound C[Si]1(C)O[Si](C)(C)O[Si](C)(C)O[Si](C)(C)O1 HMMGMWAXVFQUOA-UHFFFAOYSA-N 0.000 claims description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- 125000003698 tetramethyl group Chemical group [H]C([H])([H])* 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- 239000012299 nitrogen atmosphere Substances 0.000 claims description 5
- 238000004321 preservation Methods 0.000 claims description 5
- 239000003784 tall oil Substances 0.000 claims description 5
- KPUWHANPEXNPJT-UHFFFAOYSA-N disiloxane Chemical compound [SiH3]O[SiH3] KPUWHANPEXNPJT-UHFFFAOYSA-N 0.000 claims description 4
- QRUDEWIWKLJBPS-UHFFFAOYSA-N benzotriazole Chemical compound C1=CC=C2N[N][N]C2=C1 QRUDEWIWKLJBPS-UHFFFAOYSA-N 0.000 claims description 2
- 239000012964 benzotriazole Substances 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- 239000003981 vehicle Substances 0.000 claims 1
- 239000006260 foam Substances 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 7
- 238000012545 processing Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 230000002195 synergetic effect Effects 0.000 abstract description 4
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 abstract description 3
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 abstract description 3
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 abstract description 3
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 abstract description 3
- 239000005642 Oleic acid Substances 0.000 abstract description 3
- 230000036541 health Effects 0.000 abstract description 3
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 abstract description 3
- 239000003921 oil Substances 0.000 abstract description 3
- 229910001369 Brass Inorganic materials 0.000 abstract description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 abstract description 2
- 239000010951 brass Substances 0.000 abstract description 2
- 238000013329 compounding Methods 0.000 abstract description 2
- 229910052802 copper Inorganic materials 0.000 abstract description 2
- 239000010949 copper Substances 0.000 abstract description 2
- 230000001050 lubricating effect Effects 0.000 abstract description 2
- 239000002173 cutting fluid Substances 0.000 description 14
- 238000005520 cutting process Methods 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 238000001514 detection method Methods 0.000 description 7
- 238000012360 testing method Methods 0.000 description 6
- 239000004094 surface-active agent Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 238000005303 weighing Methods 0.000 description 4
- RZRNAYUHWVFMIP-KTKRTIGZSA-N 1-oleoylglycerol Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(O)CO RZRNAYUHWVFMIP-KTKRTIGZSA-N 0.000 description 2
- PHYFQTYBJUILEZ-UHFFFAOYSA-N Trioleoylglycerol Natural products CCCCCCCCC=CCCCCCCCC(=O)OCC(OC(=O)CCCCCCCC=CCCCCCCCC)COC(=O)CCCCCCCC=CCCCCCCCC PHYFQTYBJUILEZ-UHFFFAOYSA-N 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005461 lubrication Methods 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241001391944 Commicarpus scandens Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005250 beta ray Effects 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- -1 hydrocarbon radicals Chemical class 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
- 230000007480 spreading Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
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- Lubricants (AREA)
Abstract
The application discloses CNC cutting oil of a copper-aluminum composite material for a new energy automobile, and relates to the technical field of metal processing oil. The cutting oil prepared by the application comprises the following raw materials in percentage by weight: 62% -82% of base oil, 7% -17% of oleic glyceride, 15% -20% of extreme pressure agent, 0.1% -0.5% of corrosion inhibitor and 0.2% -0.8% of defoamer. According to the application, the base oil is taken as a main body, and the extreme pressure agent, the corrosion inhibitor and the defoaming agent are added to perform synergistic action, so that the smoothness of brass and red copper can be improved in the CNC processing process, meanwhile, the oleic acid glyceride and the extreme pressure agent perform synergistic action in a compounding way, the lubricating property is excellent, the heat of a cutter can be rapidly taken away, the foam generated by volatilization of the base oil is inhibited, the health of workers is protected, and the environment is protected.
Description
Technical Field
The invention relates to the technical field of metal processing oil, in particular to CNC cutting oil for a copper-aluminum composite material of a new energy automobile.
Background
The metal cutting oil plays an important role in machining, the cutting fluid is an indispensable auxiliary material in cutting, the cutting fluid can reduce cutting force and friction between a cutter and a workpiece, heat generated in a cutting area can be timely taken away, so that cutting temperature is reduced, abrasion of the cutter in the cutting process is reduced, durability of the cutter is improved, product processing quality is guaranteed, and production cost is reduced. The metal cutting fluid is formed by compounding a plurality of components according to a certain proportion, a large amount of surfactants are contained in the compounded components, foam is often generated in the high-speed and high-pressure circulating flow process of the cutting fluid in the cutting process, when the surfactants exist, the film surrounding bubbles is not easy to break due to the action of surface active substances, the foam is accumulated for a long time, the contact mode of a cutter and the cutting fluid is changed from the original solid-liquid contact mode to the solid-gas-liquid contact mode, the friction between the cutter and a workpiece is increased due to the existence of gas phase, the heat of a cutting area cannot be taken away timely, and the abrasion of the cutter in the cutting process is aggravated. Because, a certain amount of defoaming agent needs to be added to the metal cutting fluid.
However, the existing defoaming agent is added into a cutting fluid system, the defoaming agent is dissolved by a surfactant in the system, the surface spreading effect is lost, the defoaming capability of the defoaming agent is greatly weakened, when the defoaming agent is added, a good defoaming effect is shown, but after a period of time, the defoaming agent is gradually dissolved, and the defoaming effect is weakened.
Disclosure of Invention
The invention aims to provide CNC cutting oil for a copper-aluminum composite material of a new energy automobile, which solves the following technical problems:
the existing cutting oil is prevented from generating foam in the using process by adding the defoaming agent, but the defoaming agent is dissolved under the action of the surfactant, so that the defoaming stability is poor.
The aim of the invention can be achieved by the following technical scheme:
the CNC cutting oil for the copper-aluminum composite material of the new energy automobile comprises the following raw materials in percentage by weight: 62% -82% of base oil, 7% -17% of oleic glyceride, 15% -20% of extreme pressure agent, 0.1% -0.5% of corrosion inhibitor and 0.2% -0.8% of defoamer.
As a further aspect of the invention: the base oil is PAO base oil.
As a further aspect of the invention: the preparation method of the defoamer comprises the following steps:
S1: adding octamethyl cyclotetrasiloxane and tetramethyl dihydrodisiloxane into a reaction kettle, adding concentrated sulfuric acid, heating to 40-60 ℃, preserving heat for reaction for 3-6h, cooling to room temperature, adjusting pH to 6-7, filtering, and distilling under reduced pressure to obtain a component I;
S2: adding the component I, allyl polyether and toluene into a reaction bottle, heating to 90-100 ℃ in a nitrogen atmosphere, adding chloroplatinic acid solution, and reacting for 2-4h under heat preservation to obtain the defoamer.
As a further aspect of the invention: in S1, the mass ratio of the octamethyl cyclotetrasiloxane to the tetramethyl dihydro disiloxane to the concentrated sulfuric acid is 80-100:100:4-6.
As a further aspect of the invention: the chloroplatinic acid solution in S2 was 1g:10-20mL of chloroplatinic acid: mixing isopropanol to obtain the product; the addition ratio of the component I, the allyl polyether, toluene and chloroplatinic acid is 10g:2-4g:20-40mL:1-2g.
As a further aspect of the invention: the extreme pressure agent is prepared by mixing phosphate and liquid rosin with the mass ratio of 55:45.
As a further aspect of the invention: the corrosion inhibitor is any one of benzotriazole and phosphate.
As a further aspect of the invention: the preparation method of the cutting oil comprises the following steps:
B1: sequentially adding base oil, oleic glyceride and an extreme pressure agent into a reaction kettle, controlling the reaction temperature at 40-50 ℃, and stirring for 30min at a stirring speed of 400-500rpm;
B2: the reaction temperature is controlled at 35-40 ℃, then nonferrous metal corrosion inhibitor and defoamer are added into the reaction kettle in sequence, and the mixture is stirred for 30min at the stirring speed of 400-500rpm, thus obtaining the cutting oil.
The invention has the beneficial effects that:
(1) The application takes octamethyl cyclotetrasiloxane and tetramethyl dihydro disiloxane as raw materials to be added, and concentrated sulfuric acid is taken as a catalyst to prepare a component I; the component I and allyl polyether are used as raw materials to prepare the defoamer. Compared with the C-O bond and the C-C bond contained in the existing defoamer, the defoamer prepared by the application has higher bond energy, and the electronegativity of oxygen, improves the oxidation stability of hydrocarbon radicals, endows the defoamer with better heat resistance, and improves the dispersion, emulsification and stability of the defoamer in water due to the functional groups introduced by the tail end or side chain of siloxane. The defoamer prepared by the application not only endows the material with excellent self-emulsifying property and water dispersibility, but also is acid and alkali resistant; effectively avoiding the dissolution of the defoamer by the surfactant; the cutting fluid prepared by the method has good solubility in the cutting fluid, is not easy to suspend on the surface of the cutting fluid, effectively avoids the adsorption of the defoaming agent on the surface of a solid object, further effectively avoids the situation of being taken away by a workpiece, and maintains the good defoaming property of the cutting fluid.
(2) The application takes PAO base oil as a main body, the PAO base oil is water-insoluble cutting oil, has the advantages of no chlorine and sulfur, light color and low smell, and can improve the smoothness of brass and red copper in CNC processing process by adding the synergistic effect of the extreme pressure agent, the nonferrous metal corrosion inhibitor and the defoamer, and meanwhile, the oil glyceride and the extreme pressure agent are compounded and synergistic effect, so that the application has excellent lubricity, can rapidly take away the heat of a cutter, thereby inhibiting foam generated by volatilization of the base oil, protecting the health of workers and is environment-friendly.
Detailed Description
The following description will clearly and fully describe the technical solutions of the embodiments of the present invention, and it is apparent that the described embodiments are only some embodiments of the present invention, not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Example 1
The preparation method of the defoamer comprises the following steps:
s1: adding 80g of octamethyl cyclotetrasiloxane and 100g of tetramethyl dihydrodisiloxane into a reaction kettle, adding 4g of concentrated sulfuric acid, heating to 40 ℃, preserving heat for reaction for 3 hours, cooling to room temperature, adjusting pH to 6, filtering, and distilling under reduced pressure to obtain a component I;
s2: 1g of chloroplatinic acid and 20mL of isopropanol are mixed to prepare a chloroplatinic acid solution;
s3: 10g of component I, 2g of allyl polyether and 20mL of toluene are added into a reaction bottle, the temperature is raised to 90 ℃ in a nitrogen atmosphere, 1g of chloroplatinic acid solution is added, and the reaction is carried out for 2 hours under the heat preservation, so as to obtain the defoamer.
Example 2
The preparation method of the defoamer comprises the following steps:
S1: adding 90g of octamethyl cyclotetrasiloxane and 100g of tetramethyl dihydrodisiloxane into a reaction kettle, adding 5g of concentrated sulfuric acid, heating to 50 ℃, preserving heat for reaction for 3 hours, cooling to room temperature, adjusting pH to 6, filtering, and distilling under reduced pressure to obtain a component I;
s2: 1g of chloroplatinic acid and 20mL of isopropanol are mixed to prepare a chloroplatinic acid solution;
S3: 10g of component I, 3g of allyl polyether and 30mL of toluene are added into a reaction bottle, the temperature is raised to 100 ℃ in a nitrogen atmosphere, 1g of chloroplatinic acid solution is added, and the reaction is carried out for 3 hours under the heat preservation, so as to obtain the defoamer.
Example 3
The preparation method of the defoamer comprises the following steps:
S1: adding 100g of octamethyl cyclotetrasiloxane and 100g of tetramethyl dihydrodisiloxane into a reaction kettle, adding 6g of concentrated sulfuric acid, heating to 60 ℃, preserving heat for reaction for 6 hours, cooling to room temperature, adjusting pH to 6, filtering, and distilling under reduced pressure to obtain a component I;
s2: 1g of chloroplatinic acid and 20mL of isopropanol are mixed to prepare a chloroplatinic acid solution;
s3: 10g of component I, 4g of allyl polyether and 40mL of toluene are added into a reaction bottle, the temperature is raised to 100 ℃ in a nitrogen atmosphere, 1g of chloroplatinic acid solution is added, and the reaction is carried out for 4 hours under the heat preservation, so as to obtain the defoamer.
Example 4
The CNC cutting oil for the copper-aluminum composite material of the new energy automobile comprises the following raw materials in percentage by weight: 66% PAO base oil, 17% glyceryl oleate, 16% extreme pressure agent, 0.3% phosphate, 0.7% defoamer prepared in example 1. The extreme pressure agent is prepared by mixing phosphate and liquid rosin with the mass ratio of 55:45.
Example 5
A preparation method of CNC cutting oil of copper-aluminum composite materials for new energy automobiles comprises the following steps:
(1) Weighing raw materials according to the components and the proportion in the embodiment 1, sequentially adding PAO base oil, oleic glyceride and extreme pressure agent into a reaction kettle, controlling the reaction temperature at 45 ℃, stirring at 450rpm for 30min;
(2) The reaction temperature was controlled at 45℃and then the phosphate and the antifoaming agent prepared in example 1 were sequentially added to the reaction vessel at a stirring speed of 450rpm for 30 minutes to obtain cutting oil.
Example 6
The CNC cutting oil for the copper-aluminum composite material of the new energy automobile comprises the following raw materials in percentage by weight: 70% PAO base oil, 15% oleic acid glyceride, 14.5% extreme pressure agent, 0.2% phosphate, 0.3% defoamer prepared in example 2. The extreme pressure agent is prepared by mixing phosphate and liquid rosin with the mass ratio of 55:45.
Example 7
A preparation method of CNC cutting oil of copper-aluminum composite materials for new energy automobiles comprises the following steps:
(1) Weighing raw materials according to the components and the proportion in the embodiment 6, sequentially adding PAO base oil, oleic glyceride and extreme pressure agent into a reaction kettle, controlling the reaction temperature at 49 ℃, stirring at 480rpm for 30min;
(2) The reaction temperature was controlled at 49℃and then the phosphate and the antifoaming agent prepared in example 2 were sequentially added to the reaction vessel at a stirring speed of 480rpm for 30 minutes to obtain cutting oil.
Example 8
The CNC cutting oil for the copper-aluminum composite material of the new energy automobile comprises the following raw materials in percentage by weight: 60% PAO base oil, 20% glyceryl oleate, 19% extreme pressure agent, 0.4% phosphate, 0.6% defoamer prepared in example 3. The extreme pressure agent is prepared by mixing phosphate and liquid rosin with the mass ratio of 55:45.
Example 9
A preparation method of CNC cutting oil of copper-aluminum composite materials for new energy automobiles comprises the following steps:
(1) Weighing raw materials according to the components and the proportion in the embodiment 5, sequentially adding PAO base oil, oleic glyceride and extreme pressure agent into a reaction kettle, controlling the reaction temperature at 43 ℃, stirring at 410rpm for 30min;
(2) The reaction temperature was controlled at 43 ℃, and then phosphate and the antifoaming agent prepared in example 3 were sequentially added to the reaction vessel at a stirring speed of 410rpm for 30 minutes to obtain cutting oil.
Comparative example 1
The cutting oil comprises the following raw materials in percentage by weight: 66% PAO base oil, 17% oleic acid glyceride, 16% extreme pressure agent, 0.3% phosphate, 0.7%17R2 polyether.
Comparative example 2
The preparation method of the cutting oil comprises the following steps:
(1) Weighing raw materials according to the components and the proportion in comparative example 1, sequentially adding PAO base oil, oleic glyceride and extreme pressure agent into a reaction kettle, controlling the reaction temperature at 45 ℃, stirring at 450rpm for 30min;
(2) The reaction temperature is controlled at 45 ℃, then phosphate and 17R2 polyether are added into the reaction kettle in sequence, the stirring speed is 450rpm, and the cutting oil is obtained after stirring for 30 min.
Performance detection
Comparative experiments were carried out on the machining performance and the application performance of the cutting oil prepared in examples 5, 7 and 9 according to the present invention and the existing cutting oil SH-RA 202.
(1) Four ball testing machine test: according to national standard GB/T12583-1998, using a four-ball friction tester MS-10J of Xiamen astronomical company, the testing conditions are 1780rpm and 12s, the maximum seizure-free load PB value is the maximum load of the steel ball which is not seized in a lubrication state at a certain temperature and a rotating speed, and the higher the standard measured value is, the better the lubrication performance is shown; the detection results are shown in Table 1;
(2) Ambient air particulate matter PM2.5 (beta-ray method) test: according to the technical requirements and the detection method of the continuous automatic monitoring system of the HJ 653-2013 environmental air particulate matters, a DASIBI 4000 series 7201 PM2.5 analyzer and a Defender flow calibrator are utilized, the environmental temperature is 30 ℃, the relative humidity is 55%, the test time interval is 1h, and the test time lasts for 24h; the detection results are shown in table 1, the value of the detection result PM2.5 in table 1 is an average value of 24h, and the lower the value is, the smaller the smoke amount is;
(3) Defoaming property: the defoaming performance of the cutting fluid is detected according to GB/T6144, and the detection result is shown in Table 1;
(4) Defoaming stability: in order to detect the defoaming stability of the cutting fluid, the defoaming agent in the cutting fluid is detected to not only quickly destroy foam, but also prevent foam generation in a period of time, and the defoaming capability of the defoaming agent is classified into four grades: the A level-defoaming time is less than 15s; b grade-defoaming time is less than 30s; grade C-defoaming time is less than 60s; grade D-defoaming time is greater than 60s; the detection results are shown in Table 2;
table 1: examples 4, 7, 9 and comparative example 2 Performance test data
As can be seen from table 1, the base oil in the cutting oil of examples 5, 7 and 9 prepared by the application is used as a main body, and the extreme pressure agent, the corrosion inhibitor and the defoamer are added to synergistically act, so that the smoothness of the copper-aluminum composite material can be improved in the CNC processing process, meanwhile, the oleic glyceride and the extreme pressure agent are compounded to synergistically act, the lubricating property is excellent, the heat of a cutter can be rapidly taken away, the foam generated by volatilization of PAO base oil is inhibited, the health of workers is protected, and the environment is protected. The defoamer prepared by the application has excellent foam inhibition and defoaming effects.
Table 2: examples 4, 7, 9 and comparative example 2 Performance test data
0d | 3d | 7d | 30d | |
Example 5 | A | A | C | D |
Example 7 | A | A | C | C |
Example 9 | A | A | C | D |
Comparative example 2 | B | C | D | D |
As can be seen from Table 2, the defoamer prepared according to the present application has excellent defoaming stability.
The foregoing describes one embodiment of the present invention in detail, but the description is only a preferred embodiment of the present invention and should not be construed as limiting the scope of the invention. All equivalent changes and modifications within the scope of the present invention are intended to be covered by the present invention.
Claims (5)
1. The CNC cutting oil for the copper-aluminum composite material of the new energy automobile is characterized by comprising the following raw materials in percentage by weight: 62% -82% of base oil, 7% -17% of oleic glyceride, 15% -20% of extreme pressure agent, 0.1% -0.5% of corrosion inhibitor and 0.2% -0.8% of defoamer;
The preparation method of the defoamer comprises the following steps:
S1: adding octamethyl cyclotetrasiloxane and tetramethyl dihydrodisiloxane into a reaction kettle, adding concentrated sulfuric acid, heating to 40-60 ℃, preserving heat for reaction for 3-6h, cooling to room temperature, adjusting pH to 6-7, filtering, and distilling under reduced pressure to obtain a component I;
S2: adding the component I, allyl polyether and toluene into a reaction bottle, heating to 90-100 ℃ in a nitrogen atmosphere, adding chloroplatinic acid solution, and reacting for 2-4 hours under heat preservation to obtain a defoaming agent;
the preparation method of the cutting oil comprises the following steps:
B1: sequentially adding base oil, oleic glyceride and an extreme pressure agent into a reaction kettle, controlling the reaction temperature at 40-50 ℃, and stirring for 30min at a stirring speed of 400-500rpm;
B2: the reaction temperature is controlled at 35-40 ℃, then nonferrous metal corrosion inhibitor and defoamer are added into the reaction kettle in sequence, and the mixture is stirred for 30min at the stirring speed of 400-500rpm, thus obtaining the cutting oil.
2. The CNC cutting oil for the copper-aluminum composite material of the new energy automobile, which is disclosed in claim 1, is characterized in that the mass ratio of octamethyl cyclotetrasiloxane, tetramethyl dihydro disiloxane and concentrated sulfuric acid in S1 is 80-100:100:4-6.
3. The CNC cutting oil for new energy vehicles, according to claim 1, wherein the chloroplatinic acid solution in S2 is 1g:10-20mL of chloroplatinic acid: mixing isopropanol to obtain the product; the addition ratio of the component I, the allyl polyether, toluene and chloroplatinic acid is 10g:2-4g:20-40mL:1-2g.
4. The CNC cutting oil for the copper-aluminum composite material of the new energy automobile, which is disclosed in claim 1, is characterized in that the extreme pressure agent is prepared by mixing phosphate and liquid rosin in a mass ratio of 55:45.
5. The CNC cutting oil for the copper-aluminum composite material of the new energy automobile, which is disclosed in claim 1, is characterized in that the corrosion inhibitor is any one of benzotriazole and phosphate.
Priority Applications (1)
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CN115414709A (en) * | 2022-09-23 | 2022-12-02 | 江苏四新界面剂科技有限公司 | Defoaming agent for soybean protein and preparation method thereof |
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CN115414709A (en) * | 2022-09-23 | 2022-12-02 | 江苏四新界面剂科技有限公司 | Defoaming agent for soybean protein and preparation method thereof |
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