CN107557604A - Aluminum refining agent and preparation method thereof - Google Patents

Aluminum refining agent and preparation method thereof Download PDF

Info

Publication number
CN107557604A
CN107557604A CN201711035072.XA CN201711035072A CN107557604A CN 107557604 A CN107557604 A CN 107557604A CN 201711035072 A CN201711035072 A CN 201711035072A CN 107557604 A CN107557604 A CN 107557604A
Authority
CN
China
Prior art keywords
mgcl
refining agent
sif
kmgcl
alf
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201711035072.XA
Other languages
Chinese (zh)
Inventor
王博
王博一
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Bo Pu Li Mstar Technology Ltd
Original Assignee
Hunan Bo Pu Li Mstar Technology Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hunan Bo Pu Li Mstar Technology Ltd filed Critical Hunan Bo Pu Li Mstar Technology Ltd
Priority to CN201711035072.XA priority Critical patent/CN107557604A/en
Publication of CN107557604A publication Critical patent/CN107557604A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention discloses a kind of aluminum refining agent and preparation method thereof, the component of refining agent includes K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2.Wherein, K2MgCl4And KMgCl3Generate Low melting point eutectic at high temperature, form the basic substance of aluminum refining agent provided by the invention, can in aluminium liquid rapid dispersion and effectively remove molten aluminum in non-metallic inclusion;Na2SiF6And Na3AlF6Catabolite at high temperature can effectively reduce the interface wet ability between solid-oxide and aluminium liquid, promote oxide inclusion and aluminium liquid separation;Na2CO3CO is decomposed to give off in high temperature aluminium liquid2, can effectively go dehydrogenation;CaF2The surface tension of fused salt mixt can be increased, make the fused salt spheroidizing of absorbing oxide, be easy to and melt separation, and reduce solid slag and wrap loss caused by aluminium;Edge crack can be reduced during magnesium alloy high applied to casting, so as to which the life-span of the speed of extrusion and increase mould can be increased in extrudate.

Description

Aluminum refining agent and preparation method thereof
Technical field
The invention belongs to Metallic Materials Held In Shanghai technical field, is related to a kind of aluminum refining agent and preparation method thereof.
Background technology
Aluminum refining agent is a kind of white powder or granular flux for metallurgy, after plurality of inorganic salt drying process Mixed preparing forms by a certain percentage, and aluminium and its alloy together melting, is mainly used in the hydrogen removed inside aluminium liquid and swims Oxide slag inclusion, make aluminium liquid purer.
Aluminium and its alloy show to be easy to aoxidize and absorb the characteristic of gas in melting casting cycle, cause pole in aluminium liquid Gas and field trash are easily formed, stomata, shrinkage cavity and porosity, crackle, poured short and seepage etc. are a series of to be lacked so that casting produces Fall into, substantially reduce the fatigue resistance of material, plasticity, intensity and the performance such as corrosion-resistant, or even cause casting to scrap, directly affect production The quality of product, the application enabled aluminum alloy to are extremely limited, particularly aviation alloyed aluminium material, often because occur oxide-film and The metallurgical imperfections such as non-metallic inclusion bring potential safety hazard to airborne vehicle, influence the quality of airborne vehicle.Aluminum refining agent adds Enter to remove gas and various non-metallic inclusions, such as oxide, carbide and boride, so as to improve the property of casting Energy.
But existing aluminum refining agent is being refined with after purified treatment, oxide inclusion is still more.
The content of the invention
The invention provides a kind of aluminum refining agent and preparation method thereof, is refining and is purifying to solve traditional refining agent After processing, the problem of oxide inclusion is still more.
A kind of aluminum refining agent provided by the invention includes:K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3With CaF2
According to one embodiment of present invention, the K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2Press The content of mass percent is:K2MgCl4:30~45%, KMgCl3:40~55%, Na2SiF6:3~5%, Na3AlF6:2~ 5%, Na2CO3:4~6% and CaF2:2~3%.
According to one embodiment of present invention, in addition to CaMg (CO3)2And K2SiF6One or both of.
According to one embodiment of present invention, the CaMg (CO3)2And K2SiF6One or both of press quality percentage The content of ratio is 4~19%.
Present invention also offers a kind of preparation method of aluminum refining agent, for preparing above-mentioned aluminum refining agent, bag Include following steps:
Step 1:61.0% KCl and 39.0% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C of meltings, so K is made in crystallisation by cooling afterwards2MgCl4
Step 2:43.9% KCl and 56.1% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C of meltings, so KMgCl is made in crystallisation by cooling afterwards3
Step 3:Take K obtained above2MgCl4And KMgCl3, with Na2SiF6、Na3AlF6、Na2CO3And CaF2Mixing, rise Temperature is to 600~650 DEG C of meltings, and the alloy refining is made in crystallisation by cooling after being then incubated 1~2 hour at 600~650 DEG C Agent.
According to one embodiment of present invention, the K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2Press The content of mass percent is:K2MgCl4:30~45%, KMgCl3:40~55%, Na2SiF6:3~5%, Na3AlF6:2~ 5%, Na2CO3:4~6% and CaF2:2~3%.
According to one embodiment of present invention, described KCl, MgCl2、K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、 Na2CO3And CaF2It is milled to granularity and is less than 325 mesh.
A kind of aluminum refining agent provided by the invention can include the following benefits:A kind of aluminium provided by the invention closes Gold refining agent includes K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2, wherein, K2MgCl4And KMgCl3In height The lower generation Low melting point eutectic of temperature, forms the basic substance of aluminum refining agent provided by the invention, can be quick in aluminium liquid Non-metallic inclusion scattered and effectively in removal molten aluminum;Na2SiF6And Na3AlF6Catabolite at high temperature can have Effect reduces the interface wet ability between solid-oxide and aluminium liquid, promotes oxide inclusion and aluminium liquid separation;Na2CO3In high temperature CO is decomposed to give off in aluminium liquid2, can effectively go dehydrogenation;CaF2The surface tension of fused salt mixt can be increased, make absorbing oxide Fused salt spheroidizing, is easy to and melt separation, and reduces solid slag and wrap loss caused by aluminium.
Brief description of the drawings
Fig. 1 is a kind of schematic flow sheet of the preparation method of aluminum refining agent provided in an embodiment of the present invention.
Embodiment
A kind of aluminum refining agent provided in an embodiment of the present invention includes K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、 Na2CO3And CaF2, the content of said components by mass percentage is:K2MgCl4:30~45%, KMgCl3:40~55%, Na2SiF6:3~5%, Na3AlF6:2~5%, Na2CO3:4~6%, CaF2:2~3%.
With anhydrous villaumite synthetic KMgCl3And K2MgCl4Based on, KMgCl3And K2MgCl4The shape in 424 DEG C and 465 DEG C Into Low melting point eutectic, it is swift in response when in use.
Na2SiF6And Na3AlF6The characteristics of be that fusing point is of a relatively high, hygroscopicity is small, and catabolite makes solid-oxide and aluminium Interface wet ability between liquid is reduced, and slag is easily separated with aluminium liquid, and promotes the drying of slag, and still, excessive fluoride can be sent out Raw fierce exothermic reaction, produces toxic gas.Wherein Na3AlF6It is the main component for improving purification slagging-off ability, can adsorbs Aluminum oxide is dissolved, surface tension when and can improves and aluminium liquid contacts, is easy to separate with aluminium liquid.
Na2SiF6Decomposed under temperature of aluminum liquid:
Na2SiF6→2NaF+SiF4
SiF4Gas is evaporated into, plays part degasification, Na2SiF6Following reaction is produced with oxide inclusion:
Na2SiF6+2Al2O3→Na3AlF6+3SiO2+AlF3
The Na of generation3AlF6There is absorption Al2O3Effect, also can and SiO2With reference to block slag is generated, it is easy to remove.
NaF can corrode Al2O3Metal body on-Al interfaces, depart from oxide-film machinery, be dissolved among refining agent, from And have the function that efficiently to remove the gred, Trace Sodium can also be discharged and act what is gone bad.
Na2CO3CO is decomposed to give off in aluminium liquid2, bubble dehydrogenation in uphill process, simultaneously as be oxygenatedchemicals, Also the effect of exothermic mixture can be played.
A kind of aluminum refining agent provided in an embodiment of the present invention can also include CaMg (CO3)2And K2SiF6In one kind Or two kinds, wherein, CaMg (CO3)2Effect and Na2CO3Effect in aluminium liquid is similar, K2SiF6Effect and Na2SiF6Make With similar, CaMg (CO3)2And K2SiF6One or both of content by mass percentage be 4~19%.
A kind of aluminum refining agent provided in an embodiment of the present invention is that low melting point efficiently removes the gred aluminum refining agent, is applied to Inert gas-refining agent is mixed to blow purifying method, and the refining effect that inert gas-refining agent is mixed to blow purifying method is pure by inert gas itself The restriction of degree, although using strict purification measures, also always contain a certain amount of moisture and oxygen, this gas is blown into After aluminium liquid, thin and compact oxide-film can be formed in the bubble surface being blown into, so as to hinder the hydrogen in melt to enter in bubble, is made Outgassing rate is had a greatly reduced quality.
If a certain amount of aluminum refining agent provided in an embodiment of the present invention, gas are introduced while inert gas is blown into The refining agent film that bubble surface can be melted is surrounded, and can separate the contact of moisture and oxygen with aluminium liquid in bubble, being allowed to can not Formed oxide-film, even if there is oxide generation, can also be refined agent film and be adsorbed, can effectively remove molten aluminum, almag, Sodium, lithium and calcium in alumin(i)um zinc alloy, coordinate inert gas refining sodium content minimum can be reduced into below 1ppm in casting, And various non-metallic inclusions can be removed, such as oxide, carbide and boride, efficiently removing for melt can be greatly increased Slag degassing effect, so as to effectively improve the effect of refining.
The efficient slagging-off ability of refining agent be by suction-operated of the refining agent to oxide inclusion in melt and dissolution, And mutual chemical action is determined.
Because oxide inclusion is not wetted by aluminum, the interfacial tension between the two is very big, and the embodiment of the present invention carries It is wetting to oxide inclusion for low melting point refining agent, and interfacial tension between the two is very small, in refining agent absorption melt Oxide inclusion after, the surface free energy of system can be made reduce, therefore, the refining agent has the energy of automatic absorbing oxide inclusion Power, meanwhile, and because the interfacial tension of the refining agent and aluminium liquid is very big, it is good with absorption property, and the ability that efficiently removes the gred is strong, The characteristics of aluminium slag good separating effect.
Low melting point refining agent degasification feature is mainly manifested in three aspects:
(1) refining agent is with oxidizing slag, such as γ-Al2O3Complex compound γ-the Al of formation2O3XH removing, and remove by oxygen Change and be mingled with absorbed part complexing H;
(2) refining agent, which produces, decomposes or forms gaseous products when being interacted with melt, so as to be diffused dehydrogenation;
(3) atomic hydrogen of dissolving is caused to become to be more prone to Atmospheric Diffusion because bath surface oxide-film is dissolved.
The embodiment of the present invention additionally provides a kind of preparation method of aluminum refining agent, for preparing above-mentioned alloy refining Agent, it is a kind of flow chart of the preparation method of aluminum refining agent provided in an embodiment of the present invention referring to Fig. 1, including following step Suddenly:
Step 1:Step 1:61.0% KCl and 39.0% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C Melt, then K is made in crystallisation by cooling2MgCl4
Step 2:43.9% KCl and 56.1% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C of meltings, so KMgCl is made in crystallisation by cooling afterwards3
Step 3:Take K obtained above2MgCl4And KMgCl3, with Na2SiF6、Na3AlF6、Na2CO3And CaF2Mixing, rise Temperature is to 600~650 DEG C of meltings, and aluminum refining agent is made in crystallisation by cooling after being then incubated 1~2 hour at 600~650 DEG C.
Wherein, K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2Content by mass percentage is: K2MgCl4:30~45%, KMgCl3:40~55%, Na2SiF6:3~5%, Na3AlF6:2~5%, Na2CO3:4~6% Hes CaF2:2~3%.
Detailed preparation process is illustrated with embodiment below.
Embodiment 1
Step 1:Weigh 18.3kg KCl and 11.7kg MgCl2Mixing and ball milling to granularity is less than 325 mesh, heats up 500 DEG C and melts Melt, crystallized after cooling, 30kg K are made in the particle for being crushed to 2~5mm2MgCl4
Step 2:Weigh 24.1kg KCl and 30.9kg MgCl2, first by 24.1kg KCl and 15.4kg MgCl2Mixing It is milled to granularity and is less than 325 mesh, is warming up to 500 DEG C of meltings, adds remaining 15.5kg MgCl2Until all meltings, cooling After crystallize, 55kg KMgCl are made in the particle for being crushed to 5~10mm3
Step 3:Weigh 30kg K2MgCl4、55kg KMgCl3、3kg Na2SiF6、5kg Na3AlF6、4kg Na2CO3With 3kg CaF2, above several material mixing and ball millings to 325 mesh, 600~650 DEG C of meltings will be warming up to, 1 is incubated at 600~650 DEG C Remove the crystallization water within~2 hours, crystallized after cooling, the aluminium conjunction that the embodiment of the present invention 1 provides is made after being crushed to 2~5mm particle Gold refining agent.
Embodiment 2
Step 1:Weigh 27.5kg KCl and 17.5kg MgCl2Mixing and ball milling to granularity is less than 325 mesh, heats up 500 DEG C and melts Melt, crystallized after cooling, be crushed to the obtained 45kg K of 2~5mm particles2MgCl4
Step 2:Weigh KCl 17.6kg and 22.4kg MgCl2, first by 17.6kg KCl and 11.2kg MgCl2Mixing It is milled to granularity and is less than 325 mesh, is warming up to 500 DEG C of meltings, adds remaining 11.2kg MgCl2Until all meltings, cooling After crystallize, 40kg KMgCl are made in the particle for being crushed to 2~5mm3
Step 3:Weigh 45kg K2MgCl4、40kg KMgCl3、5kg Na2SiF6、2kg Na3AlF6、6kg Na2CO3With 2kg CaF2, above several material mixing and ball millings to 325 mesh, 600~650 DEG C of meltings will be warming up to, 1 is incubated at 600~650 DEG C Remove the crystallization water within~2 hours, crystallized after cooling, the aluminium conjunction that the embodiment of the present invention 2 provides is made after being crushed to 2~5mm particle Gold refining agent.
Embodiment 3
Step 1:Weigh 22.9kg KCl and 14.6kg MgCl2Mixing and ball milling to granularity is less than 325 mesh, heats up 500 DEG C and melts Melt, crystallized after cooling, 37.5kg K are made in the particle for being crushed to 2~5mm2MgCl4
Step 2:Weigh 20.9kg KCl and 26.6kg MgCl2, first by 20.9kg KCl and 13.3kg MgCl2Mixing It is milled to granularity and is less than 325 mesh, is warming up to 500 DEG C of meltings, adds remaining 13.3kg MgCl2Until all meltings, cooling After crystallize, 47.5kg KMgCl are made in the particle for being crushed to 2~5mm3
Step 3:Weigh 37.5kg K2MgCl4、47.5kg KMgCl3、4kg Na2SiF6、3.5kg Na3AlF6、5kg Na2CO3With 2.5kg CaF2, will more than several material mixing and ball millings to 325 mesh, be warming up to 600~650 DEG C of meltings, 600~ 650 DEG C of insulations remove the crystallization water in 1~2 hour, are crystallized after cooling, and the embodiment of the present invention 3 is made after being crushed to 2~5mm particle The aluminum refining agent of offer.
In summary, a kind of aluminum refining agent provided in an embodiment of the present invention includes K2MgCl4、KMgCl3、Na2SiF6、 Na3AlF6、Na2CO3And CaF2, wherein, K2MgCl4And KMgCl3Low melting point eutectic is generated at high temperature, is formed the present invention and is provided Aluminum refining agent basic substance, can in aluminium liquid rapid dispersion and effectively remove molten aluminum in nonmetal inclusion Thing;Na2SiF6And Na3AlF6Catabolite at high temperature can effectively reduce the interface profit between solid-oxide and aluminium liquid It is moist, promote oxide inclusion and aluminium liquid separation;Na2CO3CO is decomposed to give off in high temperature aluminium liquid2, can effectively go dehydrogenation; CaF2The surface tension of fused salt mixt can be increased, make the fused salt spheroidizing of absorbing oxide, be easy to and melt separation, reduction are solid Slag wrap aluminium and caused by loss.
In addition, applied to inert gas-refining agent is mixed blow purifying method when, chlorine can be substituted to carry out furnace refining, reduced The use of chlorine in refining process;Edge crack can be reduced in the high magnesium alloy of casting, so that can in extrudate Increase the speed of extrusion and the life-span of increase mould.
Invention described above embodiment is not intended to limit the scope of the present invention..

Claims (7)

  1. A kind of 1. aluminum refining agent, it is characterised in that including:K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3With CaF2
  2. 2. aluminum refining agent according to claim 1, it is characterised in that the K2MgCl4、KMgCl3、Na2SiF6、 Na3AlF6、Na2CO3And CaF2Content by mass percentage is:K2MgCl4:30~45%, KMgCl3:40~55%, Na2SiF6:3~5%, Na3AlF6:2~5%, Na2CO3:4~6% and CaF2:2~3%.
  3. 3. aluminum refining agent according to claim 1, it is characterised in that also including CaMg (CO3)2And K2SiF6In one Kind or two kinds.
  4. 4. aluminum refining agent according to claim 3, it is characterised in that the CaMg (CO3)2And K2SiF6In one kind Or two kinds of contents by mass percentage are 4~19%.
  5. 5. a kind of preparation method of aluminum refining agent, for preparing the aluminum refining agent described in claim 1, its feature exists In comprising the following steps:
    Step 1:61.0% KCl and 39.0% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C of meltings, Ran Houleng But crystallize and K is made2MgCl4
    Step 2:43.9% KCl and 56.1% MgCl are taken by mass percentage2Mixing, is warming up to 500 DEG C of meltings, Ran Houleng But crystallize and KMgCl is made3
    Step 3:Take K obtained above2MgCl4And KMgCl3, with Na2SiF6、Na3AlF6、Na2CO3And CaF2Mixing, is warming up to 600~650 DEG C of meltings, the aluminum refining agent is made in crystallisation by cooling after being then incubated 1~2 hour at 600~650 DEG C.
  6. 6. the preparation method of aluminum refining agent according to claim 5, it is characterised in that the K2MgCl4、KMgCl3、 Na2SiF6、Na3AlF6、Na2CO3And CaF2Content by mass percentage is:K2MgCl4:30~45%, KMgCl3:40~ 55%, Na2SiF6:3~5%, Na3AlF6:2~5%, Na2CO3:4~6% and CaF2:2~3%.
  7. 7. the preparation method of aluminum refining agent according to claim 5, it is characterised in that described KCl, MgCl2、 K2MgCl4、KMgCl3、Na2SiF6、Na3AlF6、Na2CO3And CaF2It is milled to granularity and is less than 325 mesh.
CN201711035072.XA 2017-10-30 2017-10-30 Aluminum refining agent and preparation method thereof Pending CN107557604A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711035072.XA CN107557604A (en) 2017-10-30 2017-10-30 Aluminum refining agent and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711035072.XA CN107557604A (en) 2017-10-30 2017-10-30 Aluminum refining agent and preparation method thereof

Publications (1)

Publication Number Publication Date
CN107557604A true CN107557604A (en) 2018-01-09

Family

ID=61032160

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711035072.XA Pending CN107557604A (en) 2017-10-30 2017-10-30 Aluminum refining agent and preparation method thereof

Country Status (1)

Country Link
CN (1) CN107557604A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111041264A (en) * 2020-01-16 2020-04-21 深圳市新星轻合金材料股份有限公司 Preparation method of aluminum alloy refining agent
CN111072048A (en) * 2020-01-16 2020-04-28 深圳市新星轻合金材料股份有限公司 K2MgCl4Preparation method of (1)
CN111118327A (en) * 2020-01-16 2020-05-08 深圳市新星轻合金材料股份有限公司 K3Mg2Cl7Preparation method of (1)
CN111155010A (en) * 2020-01-16 2020-05-15 深圳市新星轻合金材料股份有限公司 Preparation method of magnesium-aluminum-titanium alloy
CN111233013A (en) * 2020-01-16 2020-06-05 深圳市新星轻合金材料股份有限公司 KMgCl3Preparation method of (1)
CN113214801A (en) * 2021-05-19 2021-08-06 中国科学院上海应用物理研究所 Low cost MgCl based on bischofite2Preparation method of (E) -KCl eutectic salt

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100006186A1 (en) * 2004-09-24 2010-01-14 Alcan Rhenalu Aluminum alloy products with high toughness and production process thereof
CN102041396A (en) * 2010-10-28 2011-05-04 湖南晟通科技集团有限公司 Preparation method of scouring agent for aluminum and aluminum alloy
CN102226239A (en) * 2011-06-14 2011-10-26 华南理工大学 Refining flux used for purifying and processing aluminum or aluminum alloy melt, and its preparation method
CN102312104A (en) * 2011-10-14 2012-01-11 南南铝业股份有限公司 Refining agent for aluminium and aluminium alloy melting
CN103088232A (en) * 2011-11-01 2013-05-08 江西永特合金有限公司 Flux used in aluminum and alloy melt processing, and preparation method thereof
CN104120293A (en) * 2014-06-13 2014-10-29 Smc(中国)有限公司 Refining composition and smelting method of aluminum or aluminum alloy
CN105087991A (en) * 2015-08-24 2015-11-25 重庆旗能电铝有限公司 Method for comprehensively recycling aluminum slag in aluminum casting production

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100006186A1 (en) * 2004-09-24 2010-01-14 Alcan Rhenalu Aluminum alloy products with high toughness and production process thereof
CN102041396A (en) * 2010-10-28 2011-05-04 湖南晟通科技集团有限公司 Preparation method of scouring agent for aluminum and aluminum alloy
CN102226239A (en) * 2011-06-14 2011-10-26 华南理工大学 Refining flux used for purifying and processing aluminum or aluminum alloy melt, and its preparation method
CN102312104A (en) * 2011-10-14 2012-01-11 南南铝业股份有限公司 Refining agent for aluminium and aluminium alloy melting
CN103088232A (en) * 2011-11-01 2013-05-08 江西永特合金有限公司 Flux used in aluminum and alloy melt processing, and preparation method thereof
CN104120293A (en) * 2014-06-13 2014-10-29 Smc(中国)有限公司 Refining composition and smelting method of aluminum or aluminum alloy
CN105087991A (en) * 2015-08-24 2015-11-25 重庆旗能电铝有限公司 Method for comprehensively recycling aluminum slag in aluminum casting production

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111041264A (en) * 2020-01-16 2020-04-21 深圳市新星轻合金材料股份有限公司 Preparation method of aluminum alloy refining agent
CN111072048A (en) * 2020-01-16 2020-04-28 深圳市新星轻合金材料股份有限公司 K2MgCl4Preparation method of (1)
CN111118327A (en) * 2020-01-16 2020-05-08 深圳市新星轻合金材料股份有限公司 K3Mg2Cl7Preparation method of (1)
CN111155010A (en) * 2020-01-16 2020-05-15 深圳市新星轻合金材料股份有限公司 Preparation method of magnesium-aluminum-titanium alloy
CN111233013A (en) * 2020-01-16 2020-06-05 深圳市新星轻合金材料股份有限公司 KMgCl3Preparation method of (1)
CN113214801A (en) * 2021-05-19 2021-08-06 中国科学院上海应用物理研究所 Low cost MgCl based on bischofite2Preparation method of (E) -KCl eutectic salt

Similar Documents

Publication Publication Date Title
CN107557604A (en) Aluminum refining agent and preparation method thereof
CN103981386B (en) Hypoeutectic and cocrystallized Al-Si alloy go bad and the method for refinement
CN102605193B (en) Refining agent for copper and copper alloy smelting
CN101643855B (en) Method for refining aluminum and aluminum alloy melt through in-situ reduction
CN109306412B (en) Refining agent for aluminum and aluminum alloy and preparation method thereof
CN103088232A (en) Flux used in aluminum and alloy melt processing, and preparation method thereof
CN102286667B (en) Sodium-free refining agent for aluminum and aluminum alloy and production method thereof
CN104328299A (en) Flux for aluminum and aluminum alloy melt refining and preparation method of flux
CN104818398B (en) Wheel hub aluminium alloy and preparation method thereof and aluminium alloy wheel hub
CN105316510B (en) A kind of aluminum refining agent containing rare earth
CN105803215B (en) Remove the multiple-effect composite refining flux of impurity and its application in aluminium and aluminium alloy melt
CN105624448B (en) Melting cast aluminum alloy flux of deslagging refining containing rare earth and preparation method thereof
CN102764879A (en) High-aluminum steel die casting protective slag
CN109536765B (en) Granular flux for aluminum alloy processing and preparation method thereof
CN102041396A (en) Preparation method of scouring agent for aluminum and aluminum alloy
CN106498216B (en) A kind of preparation method of villaumite fusion refining agent
CN105316513B (en) A kind of aluminium alloy sodium-free refining agent of the erbium of yttrium containing cerium
CN113174506A (en) Refining flux suitable for magnesium-lithium alloy and preparation method thereof
JP2006282498A (en) Method for producing high purity silicon
CN115896469A (en) Deep degassing, impurity removing and purifying method for electrical aluminum alloy liquid
CN105369044B (en) A kind of aluminium alloy sodium-free refining agent of the erbium of lanthanum containing cerium
RU2475334C2 (en) Method of making conditioning agent for hypoeutectic aluminium-silicon alloys
CN103233138A (en) Grain refiner for magnesium-aluminum (Mg-Al) magnesium alloy and preparation method thereof
CN105177311A (en) Sodium-chloride-salt-containing fusion used for aluminum melt treatment and production method of sodium-chloride-salt-containing fusion
CN113430412A (en) Protective flux for aluminum-lithium alloy and preparation method thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20180109

RJ01 Rejection of invention patent application after publication