CN109536784B - Water draining chamber - Google Patents
Water draining chamber Download PDFInfo
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- CN109536784B CN109536784B CN201811433896.7A CN201811433896A CN109536784B CN 109536784 B CN109536784 B CN 109536784B CN 201811433896 A CN201811433896 A CN 201811433896A CN 109536784 B CN109536784 B CN 109536784B
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- alloy liquid
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- type polysilsesquioxane
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 239000000956 alloy Substances 0.000 claims abstract description 113
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 112
- 229920000734 polysilsesquioxane polymer Polymers 0.000 claims abstract description 63
- 229910000838 Al alloy Inorganic materials 0.000 claims abstract description 24
- 239000002994 raw material Substances 0.000 claims abstract description 24
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 10
- 238000003723 Smelting Methods 0.000 claims abstract description 9
- 239000012535 impurity Substances 0.000 claims abstract description 9
- 229910052726 zirconium Inorganic materials 0.000 claims abstract description 9
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 8
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 8
- 239000007788 liquid Substances 0.000 claims description 73
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 30
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 30
- 229910002804 graphite Inorganic materials 0.000 claims description 30
- 239000010439 graphite Substances 0.000 claims description 30
- 239000011889 copper foil Substances 0.000 claims description 29
- 238000007873 sieving Methods 0.000 claims description 24
- 239000002245 particle Substances 0.000 claims description 21
- 239000011261 inert gas Substances 0.000 claims description 20
- 238000001816 cooling Methods 0.000 claims description 14
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 12
- 238000002156 mixing Methods 0.000 claims description 8
- 239000001307 helium Substances 0.000 claims description 7
- 229910052734 helium Inorganic materials 0.000 claims description 7
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 7
- 238000003754 machining Methods 0.000 claims description 7
- 238000002844 melting Methods 0.000 claims description 7
- 230000008018 melting Effects 0.000 claims description 7
- 239000002002 slurry Substances 0.000 claims description 7
- 238000005303 weighing Methods 0.000 claims description 7
- 229910052786 argon Inorganic materials 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 6
- 229910052754 neon Inorganic materials 0.000 claims description 5
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000010865 sewage Substances 0.000 claims description 2
- 238000005273 aeration Methods 0.000 claims 1
- 230000007797 corrosion Effects 0.000 abstract description 9
- 238000005260 corrosion Methods 0.000 abstract description 9
- 239000007769 metal material Substances 0.000 abstract description 2
- 239000000463 material Substances 0.000 description 11
- 239000011248 coating agent Substances 0.000 description 10
- 238000000576 coating method Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 229910000846 In alloy Inorganic materials 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 6
- 239000008187 granular material Substances 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000000498 cooling water Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- 239000010954 inorganic particle Substances 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 230000005653 Brownian motion process Effects 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910001128 Sn alloy Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 229910000905 alloy phase Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005537 brownian motion Methods 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000004925 denaturation Methods 0.000 description 1
- 230000036425 denaturation Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C21/00—Alloys based on aluminium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/10—Alloys containing non-metals
- C22C1/1005—Pretreatment of the non-metallic additives
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/10—Alloys containing non-metals
- C22C1/1036—Alloys containing non-metals starting from a melt
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C1/00—Making non-ferrous alloys
- C22C1/10—Alloys containing non-metals
- C22C1/1036—Alloys containing non-metals starting from a melt
- C22C1/1047—Alloys containing non-metals starting from a melt by mixing and casting liquid metal matrix composites
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01P—COOLING OF MACHINES OR ENGINES IN GENERAL; COOLING OF INTERNAL-COMBUSTION ENGINES
- F01P11/00—Component parts, details, or accessories not provided for in, or of interest apart from, groups F01P1/00 - F01P9/00
Abstract
The invention belongs to the technical field of metal materials, and particularly relates to a lower water chamber, which is made of aluminum alloy, wherein the aluminum alloy comprises the following raw materials in percentage by mass: cage polysilsesquioxane: 0.5-2.5%, Sr: 0.02 to 0.1%, Zr: 0.15-0.25%, Mn: 0.04-0.1%, Zn: 0.07-0.14%, and the balance of Al and impurities. The alloy is prepared through the process steps of smelting, airflow stirring, curing and forming, finished products and the like, and finally obtained products have good strength, hardness, elongation and corrosion resistance and are suitable for complex use environments.
Description
Technical Field
The invention relates to a drainage chamber, and belongs to the field of metal materials.
Background
The automobile water chamber is an important component of an automobile radiator, is generally arranged at the upper part and the lower part of the radiator and is used for buffering cooling water flowing into a radiator core and conveying the cooling water cooled by the radiator to an engine again to ensure the heat dissipation effect of the engine.
The automobile water chamber can be simply divided into an upper water chamber and a lower water chamber, has single function, is mainly used for storing cooling water and assisting in heat dissipation, and is indispensable.
It follows that the transition assistance function of the lower water chamber in the radiator is also of great importance. The shape of the lower water chamber is determined during preparation, and the shape cannot be optimized, so that the service life of the lower water chamber is prolonged, and the optimization of the material of the lower water chamber is focused on, and the effective service life of the lower water chamber is fundamentally prolonged. The aluminum alloy has better performance.
The aluminum alloy is an alloy system which is formed by adding a certain amount of additive elements such as metal/nonmetal and the like on the basis of aluminum and controlling the content of impurity elements. The aluminum alloy has the advantages of high strength, high hardness, corrosion resistance and light weight, and is suitable for being used as a structural material. But the material composition and smelting process of the traditional aluminum alloy cannot better improve the alloy performance.
In order to overcome the defects of low hardness, poor wear resistance and the like of the traditional alloy, the publication No. CN102121414A discloses an all-aluminum alloy heavy truck water tank, which utilizes aluminum alloy to replace plastic and is made into a water tank through structural change, so that the service life of the water tank is prolonged, the pollution of plastic manufacture to the environment is reduced, and the maintenance and use cost of a user is reduced. However, such a simple material replacement is prone to defects in the manufacturing process, and cannot fundamentally change the performance of the water chamber, and even cannot cope with a complicated use environment.
Disclosure of Invention
In view of the problems, the invention provides a sewage chamber which has higher strength, high hardness and corrosion resistance and can adapt to complex environment.
In order to achieve the purpose, the invention adopts the following technical scheme:
the lower water chamber is made of aluminum alloy, and the aluminum alloy comprises the following raw materials in percentage by mass: cage polysilsesquioxane: 0.5-2.5%, Sr: 0.02 to 0.1%, Zr: 0.15-0.25%, Mn: 0.04-0.1%, Zn: 0.07-0.14%, and the balance of Al and impurities.
Preferably, the cage-type polysilsesquioxane is in the form of particles, and the particle size of the cage-type polysilsesquioxane is 0.5-1.5 mm.
Further preferably, each particle of the cage-type polysilsesquioxane is coated with a copper foil, and the coating form is half-coating or full-coating.
More preferably, the thickness of the copper foil is 6-10 μm, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 20-30: 1.
According to the invention, cage type polysilsesquioxane is specially added into an aluminum alloy material, the basic attribute of the cage type polysilsesquioxane belongs to inorganic particles, but the silicon element has extensibility and metallicity, and the cage type polysilsesquioxane can be well blended into the aluminum alloy as a reinforcing component in the test process. In the process of developing the aluminum alloy, the whisker growth phenomenon of different degrees can exist when different elements in the aluminum alloy are mixed to form components, the performance of the alloy can be affected to different degrees by excessive growth, microcracks are easily generated after the alloy is formed, the service life of products produced by the alloy is shortened, and meanwhile, the grain refinement is not facilitated, so that the reduction of synthetic metal (such as strength, hardness, resistance and the like) is caused. The power of whisker growth is from oxidation of trace oxygen in the alloy to part of the added elements to generate oxides to further cause volume expansion and generate compressive stress to other surrounding phases, and the cage-type polysilsesquioxane can greatly relieve the oxidation process of the added elements and inhibit the generation of the oxides of the added elements, thereby slowing the whisker growth. The particle size of the cage-type polysilsesquioxane is limited so as to be better blended into the alloy components and avoid layering (insufficient blending) due to too large particle size.
Meanwhile, the cage-type polysilsesquioxane can promote the modification effect of Sr and Zr elements on the alloy, the tensile strength of the alloy at room temperature is improved by more than 25% compared with that before modification, and the Sr element is more easily enriched on the surface layer of the alloy, so that the corrosion resistance of the alloy is further enhanced, and the lower water chamber can deal with the corrosion force generated by cooling water at different temperature differences.
Considering that the inorganic particle property of the cage type polysilsesquioxane is slightly higher than the metal property of the cage type polysilsesquioxane, the copper foil coating treatment is carried out on the outer layer of the cage type polysilsesquioxane, the thickness and the using amount of the copper foil are limited, and the combination degree of the cage type polysilsesquioxane and the alloy can be fully ensured by the copper foil with smaller thickness and lower content. Meanwhile, trace copper element can also enhance the comprehensive performance of the alloy.
The invention also provides another technical scheme while reasonably selecting the material proportion:
a preparation method of a lower water chamber comprises the following steps:
(1) smelting: weighing the raw materials, and mixing and melting all the raw materials except the cage-type polysilsesquioxane to form alloy liquid;
(2) airflow stirring: introducing inert gas into the alloy liquid from the side surface of the alloy liquid, and circulating and repeatedly sieving the alloy liquid from the side surface of the alloy liquid by using a graphite net;
(3) curing and forming: slowly reducing the temperature, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
(4) and (3) finished product: and machining the alloy block to form the water outlet chamber.
In the preparation process of the lower water chamber, the invention particularly adopts an alloy processing technology of airflow stirring. The air flow stirring is a mode of combining air flow and stirring, strong convection is generated on the alloy liquid by utilizing the air flow, and alloy crystal grains are refined by utilizing a stirring mode of sieving a graphite net, so that a semi-solid structure with good performance is formed, and the elongation of the alloy is greatly enhanced.
Preferably, the temperature during the gas flow stirring is controlled at 600-650 ℃, and the cooling is carried out by using soft metal (such as gallium-indium alloy, tin alloy and the like) during the solidification. The slower cooling rate is kept, so that the cage-type polysilsesquioxane particles can be protected from partial denaturation and partial solidification due to larger temperature difference to form an alloy with non-uniform components.
Preferably, the inert gas in step (2) comprises one or more of argon, helium and neon.
Preferably, in the step (2), bubbles are formed on the upper surface of the alloy liquid without breaking when the gas is introduced from the side.
When gas is introduced, the alloy liquid is in a strong convection and strong stirring state due to the action of bubbles. At this time, the bubbles generate turbulence and apply shear stress to the alloy liquid. In turbulent flow, fluid particles make brownian motion, which causes momentum exchange between different metallic fluid phase particles, thereby creating greater shear stress and losing more efficiency. I.e. to optimize the morphology of the alloy structure.
Preferably, the grid height of the graphite net in the step (2) is not more than the upper surface of the alloy liquid.
Preferably, the inert gas rate in the step (2) is consistent with the sieving rate of the graphite net, and both the inert gas rate and the sieving rate are 0.5-1.5 cm/s.
No matter the bubbling is controlled not to be broken, or the height of the graphite net is not more than the upper surface of the alloy liquid, the purpose is to control the inert gas not to be dissipated from the upper surface of the alloy liquid, so that the structure phase of the alloy is layered, and the outermost alloy phase has higher corrosion resistance.
Compared with the prior art, the invention has the following advantages:
(1) the invention specially adds the cage type polysilsesquioxane as a reinforcing component and inhibits the growth of whiskers.
(2) According to the invention, the copper foil coating treatment is carried out on the outer layer of the cage-type polysilsesquioxane, the thickness and the using amount of the copper foil are limited, and the combination degree of the cage-type polysilsesquioxane and the alloy can be fully ensured by the copper foil with smaller thickness and lower content.
(3) The invention particularly adopts an alloy processing technology of airflow stirring, namely, a mode of combining airflow and stirring is adopted, the airflow is utilized to generate strong convection to alloy liquid, and a stirring mode of sieving a graphite mesh is utilized to refine alloy grains, so that a semi-solid structure with good performance is formed, and the elongation of the alloy is greatly enhanced.
Detailed Description
The following are specific examples of the present invention and further describe the technical solutions of the present invention, but the present invention is not limited to these examples.
Example 1
Preparing materials: weighing the raw materials according to the proportion of the aluminum alloy, wherein the raw materials comprise cage type polysilsesquioxane: 1.5%, Sr: 0.06%, Zr: 0.2%, Mn: 0.07%, Zn: 0.1 percent of Al and impurities, wherein the cage-type polysilsesquioxane is granular, the particle size is 1mm, each granule of the cage-type polysilsesquioxane is coated with a semi-coating copper foil, the thickness of the copper foil is controlled to be 8 mu m, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 25: 1;
smelting: mixing and melting all raw materials except the cage-type polysilsesquioxane to form alloy liquid;
airflow stirring: controlling the temperature of the alloy liquid to be 630 ℃, introducing mixed gas of argon, helium and neon into the alloy liquid from the lateral surface of the alloy liquid, keeping the upper surface of the alloy liquid to form unbroken bubbles, and meanwhile, circularly and repeatedly sieving the alloy liquid from the lateral surface of the alloy liquid by using a graphite net with the grid height not exceeding the upper surface of the alloy liquid, keeping the speed of inert gas consistent with the sieving speed of the graphite net, wherein the speed of inert gas is 1 cm/s;
curing and forming: slowly cooling the alloy liquid by utilizing the gallium-indium alloy, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
and (3) finished product: and machining the alloy block to form the water outlet chamber.
Example 2
Preparing materials: weighing the raw materials according to the proportion of the aluminum alloy, wherein the raw materials comprise cage type polysilsesquioxane: 0.5%, Sr: 0.02%, Zr: 0.15%, Mn: 0.04%, Zn: 0.07 percent of Al and impurities, wherein the cage-type polysilsesquioxane is granular, the grain diameter is 0.5mm, each granule of the cage-type polysilsesquioxane is coated with a semi-coating copper foil, the thickness of the copper foil is controlled to be 6 mu m, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 20: 1;
smelting: mixing and melting all raw materials except the cage-type polysilsesquioxane to form alloy liquid;
airflow stirring: controlling the temperature of the alloy liquid to be 630 ℃, introducing mixed gas of argon, helium and neon into the alloy liquid from the lateral surface of the alloy liquid, keeping the upper surface of the alloy liquid to form unbroken bubbles, and meanwhile, circularly and repeatedly sieving the alloy liquid from the lateral surface of the alloy liquid by using a graphite net with the grid height not exceeding the upper surface of the alloy liquid, keeping the speed of inert gas consistent with the sieving speed of the graphite net, wherein the speed of inert gas is 1 cm/s;
curing and forming: slowly cooling the alloy liquid by utilizing the gallium-indium alloy, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
and (3) finished product: and machining the alloy block to form the water outlet chamber.
Example 3
Preparing materials: weighing the raw materials according to the proportion of the aluminum alloy, wherein the raw materials comprise cage type polysilsesquioxane: 2.5%, Sr: 0.1%, Zr: 0.25%, Mn: 0.1%, Zn: 0.14 percent of Al and impurities, wherein the cage-type polysilsesquioxane is granular, the grain diameter is 1.5mm, each granule of the cage-type polysilsesquioxane is coated with a copper foil in a full coating mode, the thickness of the copper foil is controlled to be 10 mu m, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 30: 1;
smelting: mixing and melting all raw materials except the cage-type polysilsesquioxane to form alloy liquid;
airflow stirring: controlling the temperature of the alloy liquid to be 630 ℃, introducing mixed gas of argon, helium and neon into the alloy liquid from the lateral surface of the alloy liquid, keeping the upper surface of the alloy liquid to form unbroken bubbles, and meanwhile, circularly and repeatedly sieving the alloy liquid from the lateral surface of the alloy liquid by using a graphite net with the grid height not exceeding the upper surface of the alloy liquid, keeping the speed of inert gas consistent with the sieving speed of the graphite net, wherein the speed of inert gas is 1 cm/s;
curing and forming: slowly cooling the alloy liquid by utilizing the gallium-indium alloy, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
and (3) finished product: and machining the alloy block to form the water outlet chamber.
Example 4
Preparing materials: weighing the raw materials according to the proportion of the aluminum alloy, wherein the raw materials comprise cage type polysilsesquioxane: 1.5%, Sr: 0.06%, Zr: 0.2%, Mn: 0.07%, Zn: 0.1 percent of Al and impurities, wherein the cage-type polysilsesquioxane is granular, the particle size is 1mm, each granule of the cage-type polysilsesquioxane is coated with a semi-coating copper foil, the thickness of the copper foil is controlled to be 8 mu m, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 25: 1;
smelting: mixing and melting all raw materials except the cage-type polysilsesquioxane to form alloy liquid;
airflow stirring: controlling the temperature of the alloy liquid to be 600 ℃, introducing mixed gas of argon and helium into the alloy liquid from the lateral surface of the alloy liquid, keeping the upper surface of the alloy liquid to form an unbroken bubble, and simultaneously circularly and repeatedly sieving from the lateral surface of the alloy liquid by using a graphite net with the grid height not exceeding the upper surface of the alloy liquid, wherein the speed of inert gas is kept consistent with the sieving speed of the graphite net, and the speed is 0.5 cm/s;
curing and forming: slowly cooling the alloy liquid by utilizing the gallium-indium alloy, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
and (3) finished product: and machining the alloy block to form the water outlet chamber.
Example 5
Preparing materials: weighing the raw materials according to the proportion of the aluminum alloy, wherein the raw materials comprise cage type polysilsesquioxane: 1.5%, Sr: 0.06%, Zr: 0.2%, Mn: 0.07%, Zn: 0.1 percent of Al and impurities, wherein the cage-type polysilsesquioxane is granular, the particle size is 1mm, each granule of the cage-type polysilsesquioxane is coated with a semi-coating copper foil, the thickness of the copper foil is controlled to be 8 mu m, and the volume ratio of the cage-type polysilsesquioxane to the copper foil is 25: 1;
smelting: mixing and melting all raw materials except the cage-type polysilsesquioxane to form alloy liquid;
airflow stirring: controlling the temperature of the alloy liquid to be 650 ℃, introducing helium into the alloy liquid from the side surface of the alloy liquid, keeping the upper surface of the alloy liquid to form an unbroken bubble, and simultaneously circularly and repeatedly sieving the alloy liquid from the side surface of the alloy liquid by using a graphite net with the grid height not exceeding the upper surface of the alloy liquid, wherein the speed of inert gas is kept consistent with the sieving speed of the graphite net, and the speed of inert gas is 1.5 cm/s;
curing and forming: slowly cooling the alloy liquid by utilizing the gallium-indium alloy, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
and (3) finished product: and machining the alloy block to form the water outlet chamber.
Example 6
The difference from the example 1 is only that the content of the cage type polysilsesquioxane in the aluminum alloy raw material of the example 6 is 0.4%.
Example 7
The difference from the example 1 is only that the content of the cage type polysilsesquioxane in the aluminum alloy raw material of the example 7 is 2.6%.
Example 8
The only difference from example 1 is that the volume ratio of the cage polysilsesquioxane to the copper foil in example 8 is 19: 1.
Example 9
The only difference from example 1 is that the volume ratio of the cage polysilsesquioxane to the copper foil in example 9 is 31: 1.
Example 10
The difference from example 1 is only that the grid height of the graphite mesh in example 10 exceeds the upper surface of the alloy liquid.
Example 11
The difference from the embodiment 1 is that the upper surface of the alloy liquid of the embodiment 11 forms a burst bubble.
Example 12
The only difference from example 1 is that the inert gas rate of example 12 does not correspond to the screening rate of the graphite mesh.
Comparative example 1
The only difference from example 1 is that the aluminum alloy composition of comparative example 1 does not contain cage polysilsesquioxane.
Comparative example 2
The only difference from example 1 is that only inert gas was introduced during the preparation of comparative example 2, and no graphite mesh screening was performed.
Comparative example 3
The only difference from example 1 is that only the graphite mesh was sieved during the preparation of comparative example 3, and no inert gas was passed.
The launching chambers of examples 1 to 12 and comparative examples 1 to 3 were tested for strength, elongation, corrosion resistance and hardness, and the results are shown in table 1:
table 1: performance of the lower water chamber in examples 1 to 12 and comparative examples 1 to 3
The corrosion resistance data in the table refers to the time when corrosion spots appear on the surface of the lower water chamber, and the changes in materials and processes have great influence on the performance of the product.
While the invention has been described in detail and with reference to specific embodiments thereof, it will be apparent to one skilled in the art that various changes and modifications can be made therein without departing from the spirit and scope thereof.
Claims (8)
1. The sewage chamber is characterized by being made of aluminum alloy, wherein the aluminum alloy comprises the following raw materials in percentage by mass: cage polysilsesquioxane: 0.5-2.5%, Sr: 0.02 to 0.1%, Zr: 0.15-0.25%, Mn: 0.04-0.1%, Zn: 0.07-0.14%, and the balance of Al and impurities;
the preparation method of the lower water chamber comprises the following steps:
(1) smelting: weighing the raw materials, and mixing and melting all the raw materials except the cage-type polysilsesquioxane to form alloy liquid;
(2) airflow stirring: introducing inert gas into the alloy liquid from the side surface of the alloy liquid, and circulating and repeatedly sieving the alloy liquid from the side surface of the alloy liquid by using a graphite net;
(3) curing and forming: slowly reducing the temperature, adding cage-type polysilsesquioxane particles when the alloy liquid is semisolid slurry, continuously sieving by using a graphite net, and naturally cooling until an alloy block is formed;
(4) and (3) finished product: and machining the alloy block to form the water outlet chamber.
2. The launching chamber as claimed in claim 1, characterized in that the cage-type polysilsesquioxane is in the form of particles having a particle size of 0.5-1.5 mm.
3. The downcomer chamber of claim 2, wherein each particle of said cage polysilsesquioxane is clad with a copper foil, the clad configuration being either half clad or full clad.
4. The drain chamber of claim 3, wherein the copper foil has a thickness of 6-10 μm, and the volume ratio of the cage polysilsesquioxane to the copper foil is 20-30: 1.
5. The method for preparing the drain chamber according to claim 1, wherein the inert gas in the step (2) includes one or more of argon, helium and neon.
6. The method for manufacturing a drain chamber according to claim 1, wherein the upper surface of the alloy liquid forms an unbroken bubble during the side-aeration in step (2).
7. The method for preparing the drain chamber according to claim 1, wherein the grid height of the graphite net in the step (2) does not exceed the upper surface of the alloy liquid.
8. The method for preparing the drain chamber according to claim 1, wherein the inert gas rate in the step (2) is consistent with the sieving rate of the graphite mesh, and is 0.5-1.5 cm/s.
Priority Applications (1)
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JP2014231620A (en) * | 2013-05-28 | 2014-12-11 | 昭和電工株式会社 | Aluminum alloy foil for electrolytic capacitor electrode |
US9321700B2 (en) * | 2011-08-04 | 2016-04-26 | University Of Utah Research Foundation | Production of nanoparticles using homogeneous milling and associated products |
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CN101871062A (en) * | 2009-04-21 | 2010-10-27 | 株式会社电装 | Aluminum alloy clad sheet for heat exchangers |
US9321700B2 (en) * | 2011-08-04 | 2016-04-26 | University Of Utah Research Foundation | Production of nanoparticles using homogeneous milling and associated products |
CN102433475A (en) * | 2011-12-15 | 2012-05-02 | 贵州华科铝材料工程技术研究有限公司 | High-strength and high-hardness aluminum alloy and preparation method thereof |
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Denomination of invention: A type of drainage chamber Effective date of registration: 20231116 Granted publication date: 20200717 Pledgee: Ningbo Yinzhou Rural Commercial Bank Co.,Ltd. Jiangshan sub branch Pledgor: NINGBO MINGFA AUTOMOBILE PARTS Co.,Ltd. Registration number: Y2023980065996 |