CN1322153C - Energy-saving continuous aluminum alloy melting-refining furnace - Google Patents
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- 238000007670 refining Methods 0.000 title claims abstract description 26
- 229910000838 Al alloy Inorganic materials 0.000 title claims abstract description 16
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 120
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 119
- 238000007872 degassing Methods 0.000 claims abstract description 55
- 239000007788 liquid Substances 0.000 claims abstract description 46
- 238000002844 melting Methods 0.000 claims abstract description 30
- 230000008018 melting Effects 0.000 claims abstract description 30
- 238000013021 overheating Methods 0.000 claims abstract description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 25
- 239000007789 gas Substances 0.000 claims description 19
- 229910052757 nitrogen Inorganic materials 0.000 claims description 12
- 238000004321 preservation Methods 0.000 claims description 12
- 238000005192 partition Methods 0.000 claims description 11
- 239000011819 refractory material Substances 0.000 claims description 4
- 239000000463 material Substances 0.000 abstract description 11
- 238000009413 insulation Methods 0.000 abstract description 9
- 230000010354 integration Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 238000005266 casting Methods 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 6
- 239000002184 metal Substances 0.000 description 6
- 230000005611 electricity Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000010309 melting process Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 239000004020 conductor Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000011112 process operation Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000002737 fuel gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003020 moisturizing effect Effects 0.000 description 1
- 229910021652 non-ferrous alloy Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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Abstract
Description
技术领域:Technical field:
本发明涉及一种连续式铝合金熔化-精炼装置,尤其是涉及一种集竖炉式预热、熔化炉料区,反射炉式铝液过热区以及坩埚炉式去气精炼、保温浇注区组成一体,除在反射炉式铝液过热区安装燃油或燃气燃烧器供给热量加热各个区域外,不再使用燃料或电能熔化或加热铝液,从而节省了炉料预热、熔化所需热能和铝液去气精炼、保温所需电能以及铝液运输、分送过程中的热量损失的节能型连续式铝合金熔化-精炼炉。The invention relates to a continuous aluminum alloy melting-refining device, in particular to a shaft furnace-type preheating and melting zone, a reverberatory furnace-type molten aluminum superheating zone, and a crucible furnace-type degassing and refining, heat preservation pouring zone. In addition to installing fuel oil or gas burners in the overheating area of the reverberatory furnace type aluminum liquid to heat each area, no fuel or electric energy is used to melt or heat the aluminum liquid, thus saving the heat energy required for preheating and melting of the charge and the removal of the aluminum liquid An energy-saving continuous aluminum alloy melting-refining furnace for the electric energy required for gas refining and heat preservation and the heat loss during the transportation and distribution of aluminum liquid.
背景技术:Background technique:
随着我国经济高速发展,铝制品应用日趋增多。熔铝、去气精炼、浇注是众多铝铸件第一道生产环节。一般车间往往将熔铝用的电炉或反射炉与去气保温电炉分别布置在不同的区域。铝液由反射炉/电炉或者经过流槽流入坩埚式去气炉中或者先盛在铝水包内,然后倒入电炉内调整温度和化学成份,再经过去气精炼处理后即可浇注。这样的阶段式分散的熔化系统,铝液几经转运和分送,温度多次升降,热量损失甚多,热效率甚低。通常每公斤铝液需用电0.2-0.4度才能保证、浇注等工艺顺利进行去气精炼。此外,铝液在转运过程容易氧化,生成夹杂物,降低了合金质量。当前我国电力供应紧张,如何提高熔铝系统热效率、节省电能、又能保证铸件品质一直是冶金界关注热点之一。With the rapid development of my country's economy, the application of aluminum products is increasing day by day. Melting aluminum, degassing refining, and pouring are the first production steps of many aluminum castings. In general workshops, the electric furnace or reverberatory furnace for melting aluminum and the degassing and holding electric furnace are often arranged in different areas. The molten aluminum flows into the crucible-type degassing furnace from the reverberatory furnace/electric furnace or through the launder or is first filled in the aluminum water ladle, then poured into the electric furnace to adjust the temperature and chemical composition, and then poured after degassing and refining treatment. In such a staged and dispersed melting system, the liquid aluminum is transferred and distributed several times, the temperature rises and falls many times, the heat loss is very large, and the thermal efficiency is very low. Usually, 0.2-0.4 degrees of electricity is needed per kilogram of aluminum liquid to ensure smooth degassing and refining of pouring and other processes. In addition, the molten aluminum is easily oxidized during the transfer process, and inclusions are formed, which reduces the quality of the alloy. At present, my country's power supply is tight. How to improve the thermal efficiency of the aluminum melting system, save electricity, and ensure the quality of castings has always been one of the hot spots in the metallurgical industry.
上世纪八十年代有人利用反射炉燃烧废气余热预热炉料提高热效率(R.Strassman:Aluminum furnace and preheat therefore USP04 439 145 1984年3月27日)。但仍需采用电炉调整铝液温度保证去气精炼顺利进行,不能节省电能。本申请的发明人针对这一缺点,曾将干式反射炉与去气保温炉联成一体,取消了去气保温电阻炉,简化了熔化工艺,并节省了电能。但反射炉熔池的铝液上下层温差甚大,有时高达60-70℃,容易引起铝液激烈氧化和吸气,导致铝铸件品质下降。此外,冷炉料直接加在反射炉内也容易引起铝液温度的波动,都给工艺操作带来许多困难。(节能型铝合金连续式熔化-去气炉,《特种铸造及有色合金》1996年第2期13/17页)。In the 1980s, someone used the waste heat of the reverberatory furnace to preheat the charge to improve thermal efficiency (R. Strassman: Aluminum furnace and preheat therefore USP04 439 145 March 27, 1984). However, it is still necessary to use an electric furnace to adjust the temperature of the molten aluminum to ensure the smooth progress of degassing and refining, which cannot save electric energy. In order to solve this shortcoming, the inventor of the present application integrated the dry-type reverberatory furnace with the degassing and heat-retaining furnace, canceled the degassing and heat-retaining resistance furnace, simplified the melting process, and saved electric energy. However, the temperature difference between the upper and lower layers of the molten aluminum in the reverberatory furnace pool is very large, sometimes as high as 60-70°C, which is likely to cause intense oxidation and gas absorption of the molten aluminum, resulting in a decline in the quality of aluminum castings. In addition, adding the cold charge directly into the reverberatory furnace is also likely to cause fluctuations in the temperature of the molten aluminum, which brings many difficulties to the process operation. (Energy-saving aluminum alloy continuous melting-degassing furnace, "Special Casting and Nonferrous Alloys", No. 2, 1996, p. 13/17).
八十年代末国际上出现利用竖炉熔化铝合金,以大大提高了熔铝的热效率的专利(D.Barnes,J.Bass,J.Butler,R.Mckenzie:Vertical shaft furnacemelting aluminum.USP 04844426,1986年12月10日)。这类熔化装置仍需采用电炉过热铝液,进行去气精炼操作,不能达到节电的目的。At the end of the 1980s, there was a patent in the world to melt aluminum alloy in a shaft furnace to greatly improve the thermal efficiency of molten aluminum (D.Barnes, J.Bass, J.Butler, R.Mckenzie: Vertical shaft furnacemelting aluminum. USP 04844426, 1986 December 10). This type of melting device still needs to use an electric furnace to overheat molten aluminum for degassing and refining operations, which cannot achieve the purpose of saving electricity.
几乎与此同时,国际上又出现连续式熔铝保温炉,它集竖炉、反射炉以及精炼保温炉于一体,大大简化了熔化工艺,充分利用了燃气的热量,提高了热效率。(中岛光谦:金属熔解保持炉。台湾专利公告号134093,1990年5月11日及145219,1990年11月1日。)这种熔化装置的竖炉内径为圆筒状,容易棚料。保温池的铝液温度依靠提高过热区铝液温度来维持。过热区/去气池或去气池/保温池之间的两个铝液流出/入口几乎在同一水平面上,铝液虽可畅通无阻流动,传递热量,却无足够的静置时间排除夹杂物,因此,铸件品质难以保证。詹炳财针对这些缺点提出了改进型结构。(1996年5月11日台湾专利公告号275822,用於铝材之瓦斯连续熔解保温炉之改良构造(一);ZL专利号95224445.4,1997年9月27日用于铝材的煤气连续熔化保温炉)。在去气池/保温池之间设置静置池,并在静置池/保温池之间安放蜂窝状陶瓷过滤板,防止夹杂物混入保温池。这些改进型去气保温炉内的铝液温度仍依靠提高过热区铝液温度来维持,而过滤板必须频繁调换才能过滤铝液、保证合金质量。这些措施给工艺操作带来许多困难,不能保证铸件品质和熔化过程顺利进行。因此,近些年新的连续式熔铝炉皆采用外(电或气)热式去气保温炉,调整铝液温度,并且不再采用过滤板去除铝液中的夹杂物(T.Okada,H.Yoshikawa,M.Matsuura,T.Sano,T.Hatanaka:Melting/retaining furnace for aluninum ingot。EP1136778A1,2001年9月26日及Noh.H.H:Composite melting furnace for aluminum hasa Rostolcasing coupled to the lower part of the melting tower to support theraw material and flow down molten metal。KR2003003299-A 2003年1月10日,Derwent编号2004-312071)。但这些炉型皆不能节约电能。Almost at the same time, a continuous aluminum melting and holding furnace appeared in the world. It integrates a shaft furnace, a reverberatory furnace and a refining and holding furnace, which greatly simplifies the melting process, makes full use of the heat of the gas, and improves the thermal efficiency. (Mitsuhim Nakajima: Metal Melting Holding Furnace. Taiwan Patent Publication No. 134093, May 11, 1990 and 145219, November 1, 1990.) The inner diameter of the shaft furnace of this melting device is cylindrical, and it is easy to shed materials . The temperature of the molten aluminum in the heat preservation pool is maintained by increasing the temperature of the molten aluminum in the superheated zone. The two liquid aluminum outlets/inlets between the superheated area/degassing pool or the degassing pool/insulation pool are almost at the same level. Although the aluminum liquid can flow unimpeded and transfer heat, there is not enough standing time to remove inclusions. Therefore, the quality of castings is difficult to guarantee. Zhan Bingcai proposed an improved structure for these shortcomings. (Taiwan patent announcement No. 275822 on May 11, 1996, the improved structure of the gas continuous melting and holding furnace for aluminum materials (1); ZL patent No. 95224445.4, used on September 27, 1997 for the gas continuous melting and heat preservation of aluminum materials furnace). A static pool is set between the degassing pool/insulation pool, and a honeycomb ceramic filter plate is placed between the static pool/insulation pool to prevent inclusions from mixing into the insulation pool. The temperature of the molten aluminum in these improved degassing and holding furnaces is still maintained by increasing the temperature of the molten aluminum in the overheating zone, and the filter plates must be replaced frequently to filter the molten aluminum and ensure the quality of the alloy. These measures bring many difficulties to the process operation, and cannot guarantee the casting quality and the smooth progress of the melting process. Therefore, in recent years, new continuous aluminum melting furnaces have adopted external (electric or gas) heating degassing and holding furnaces to adjust the temperature of the molten aluminum, and no longer use filter plates to remove inclusions in the molten aluminum (T.Okada, H.Yoshikawa, M.Matsuura, T.Sano, T.Hatanaka: Melting/retaining furnace for aluninum ingot. EP1136778A1, September 26, 2001 and Noh.H.H: Composite melting furnace for aluminum hasa Rostolcasing coupled to the lower part of the melting tower to support theraw material and flow down molten metal. KR2003003299-A January 10, 2003, Derwent No. 2004-312071). But none of these furnace types can save electric energy.
发明内容:Invention content:
本发明的目的在于提供一种节能型连续式铝合金熔化—精炼炉,解决集预热、熔化、去气、精炼于一体,既提高热效率、节约能耗又保证铝液质量的技术问题。The purpose of the present invention is to provide an energy-saving continuous aluminum alloy melting-refining furnace, which solves the technical problems of integrating preheating, melting, degassing and refining, improving thermal efficiency, saving energy consumption and ensuring the quality of molten aluminum.
本发明解决的上述的技术问题是通过以下方式实现的:The above-mentioned technical problem that the present invention solves is achieved in the following manner:
一种节能型连续式铝合金熔化-精炼炉,包含联成一体的由竖炉构成的炉料预熔化区、反射炉构成的铝液过热区以及坩埚炉构成的去气池和保温池三个组成部分,其特征在于:只在铝液过热区安装油料或气体燃烧器,反射炉的外炉墙为园形;呈半圆形的坩埚炉一侧延伸至反射炉外炉墙内,形成与铝液过热区分隔的公共炉墙;坩埚炉中的去气池和保温池由隔墙分开;去气池上方具有与铝液过热区相通的气流通道,与铝液过热区内熔池底部相通的铝液流入口位于去气池中部,沟通去气池与保温池的铝液通道位于隔墙底部。An energy-saving continuous aluminum alloy melting-refining furnace, which consists of three components: a charge pre-melting zone formed by a shaft furnace, an aluminum liquid overheating zone formed by a reverberatory furnace, and a degassing pool and a holding pool formed by a crucible furnace. Part, which is characterized in that: oil or gas burners are only installed in the superheated area of molten aluminum, and the outer furnace wall of the reverberatory furnace is circular; one side of the semicircular crucible furnace extends into the outer furnace wall of the reverberatory furnace, forming a The common furnace wall separated by the liquid superheating area; the degassing pool and the holding pool in the crucible furnace are separated by a partition wall; above the degassing pool, there is an air flow channel that communicates with the aluminum liquid superheating area, and communicates with the bottom of the melting pool in the aluminum liquid superheating area. The liquid aluminum flow inlet is located in the middle of the degassing pool, and the aluminum liquid channel communicating the degassing pool and the heat preservation pool is located at the bottom of the partition wall.
其特征在于:设置有将氮气通入铝液过热区的熔池和去气池内的氮气去气装置。It is characterized in that it is provided with a nitrogen degassing device that feeds nitrogen into the melting pool of the superheated area of the aluminum liquid and the degassing pool.
其特征在于:该坩埚炉与反射炉之间的公共炉墙和坩埚炉内的隔墙为导热的耐火材料。It is characterized in that: the common furnace wall between the crucible furnace and the reverberatory furnace and the partition wall in the crucible furnace are heat-conducting refractory materials.
其特征在于:该反射炉的炉墙内设置有连通铝液过热区至竖炉内炉料预熔化区的气道。It is characterized in that: the furnace wall of the reverberatory furnace is provided with an air channel connecting the superheated area of molten aluminum to the pre-melted area of charge in the shaft furnace.
本发明具有下列优点:The present invention has the following advantages:
1、能节约现有技术中去气精炼的电能消耗。1. It can save the power consumption of degassing and refining in the prior art.
2、熔池内铝液上下层温度均匀化,不需要提高过热区铝液温度,避免铝液激烈氧化和吸气。2. The temperature of the upper and lower layers of the molten aluminum in the molten pool is uniform, and there is no need to increase the temperature of the molten aluminum in the overheating zone to avoid intense oxidation and air absorption of the molten aluminum.
3、导热耐火材料隔墙保证热量由过热区传递给去气池和保温池,使铝液温度满足去气、浇注要求。3. The heat-conducting refractory material partition wall ensures that the heat is transferred from the overheating area to the degassing pool and the heat preservation pool, so that the temperature of the aluminum liquid meets the requirements of degassing and pouring.
4、铝液在去气池和保湿池内有足够的停留时间能充分去气和夹杂物。4. The aluminum liquid has enough residence time in the degassing tank and moisturizing tank to fully degas and inclusions.
5、操作方便、人力和设备投入少效率高。5. Easy to operate, less manpower and equipment investment and high efficiency.
附图说明Description of drawings
图1为本发明节能型连续式熔化-精炼炉体俯视图。Figure 1 is a top view of the energy-saving continuous melting-refining furnace body of the present invention.
图2是图1A-A剖面图。Fig. 2 is a sectional view of Fig. 1A-A.
图3为图1B-B剖面图。Fig. 3 is a sectional view of Fig. 1B-B.
具体实施方式:Detailed ways:
本发明将竖炉3、反射炉7和坩埚炉16联成一体,参见图1和2,构成了预热熔化区2、铝液过热区8、以及去气池12和保温池15,燃料(油料或煤气)燃烧器(图内未标出)只安装在反射炉7的铝液过热区8内。反射炉7为圆形,以减少炉墙向周围环境的散热损失。位于竖炉3内的预热熔化区2为腰鼓状,可以防止棚料,保证炉料均匀下落。冷金属炉料包括铝锭、回炉料以及切屑压块从竖炉3上部加料口1投入炉内,在下落过程中与上升的炉气进行热交换,温度逐渐上升,有些熔化成滴状,有些呈半熔融状态,通过竖炉3底部的通道19进入反射炉7的铝液过热区8,并经倾斜炉床20积聚在反射炉炉膛8的底部形成熔池14,燃烧器燃烧的高温炉气除加热熔池14内的铝液外,还经反射炉7的炉腔分三个方向逸出,大部份高温炉气通过通道19进入竖炉3底部,再经过预热熔化区2从出气口4排入大气。炉气上升过程中将部份热量传递给下落的铝料,加热了金属;第二部份的炉气由气道口6经开设在炉墙内的气道5也进入预热熔化区2,既加热了反射炉7的炉墙,又加热了铝炉料;少量的第三部份炉气通过气流通道9进入去气池12的上部空间加热了铝液。铝液通常在铝液过热区8停留2-3小时。在铝液过热区8内还设置有氮气去气装置(图中未表示),将氮气通入熔池14的铝液内,氮气小泡在熔池14内的铝液中不断缓慢上升,轻微搅动铝液,使上下层铝液温度均匀化,其对比情况见表1所示,效果十分明显。The present invention integrates shaft furnace 3,
表1氮气搅动对铝液过热区溶池内铝液温度梯度的影响℃Table 1 The effect of nitrogen agitation on the temperature gradient of molten aluminum in the molten aluminum superheated zone
铝液逐渐升高至适当温度,再从铝液流出口10流入去气池12。从炉门17可观察炉况,清除炉渣。The aluminum liquid is gradually raised to an appropriate temperature, and then flows into the degassing
坩埚炉16一侧由耐火导热材料制造的炉墙延伸至反射炉7内公共炉墙把它与铝液过热区8隔开,中间用耐火导热材料的隔墙11将坩埚炉16分隔成去气池12和保温池15。设置在上述公共炉墙上与铝液过热区8熔池14底部相通的铝液流入口10,位于在去气池12池壁中部(见图3)。去气池12装有氮气装置(图中未表示),可以连续或间歇对铝液进行去气操作。去气池12与保温池15之间的隔墙11下端设置有铝液流通口13。铝液流入口10与铝液流通口13不在同一高度上,也不在同一方向。这种落差保证铝液由铝液过热区8湧入去气池12后,在下降流动过程中有足够的时间(20-30分钟)与从池底上升的小氮气泡相互作用,得到去气精炼。隔墙11起到防止熔渣和夹杂物进入保温池15重新污染铝液的作用。精炼过的铝液从铝液流通口13进入保温池15底部,在铝液上升的过程中有足够的时间(40-50分钟)继续排除夹杂物。最后,清洁的铝液上升至液面,可供浇注。去气池上部一侧有气流通道9与过热区相通。这样,去气池12和保温池15中的铝液可以从以下三个方面获得热量,One side of the
(1)大量高温铝熔体不断由过铝液热区8涌入去气池,带来了热量;(1) A large amount of high-temperature aluminum melt continuously pours into the degassing pool from the molten aluminum
(2)高温炉气从气流通道9进入去气池12上部空间,加热了金属熔体;(2) The high-temperature furnace gas enters the upper space of the
(3)铝液过热区炉膛和溶池14的热量通过与坩埚炉16共有的导热材料炉墙传输到各池铝液,加热了金属熔体,有效地减缓了铝液温度的下降,保证它们具有适当的温度滿足各工艺需要。(3) The heat of the molten aluminum superheating zone furnace and the
下面通过具体实施例,进一步阐述本发明的实质性特点和显著的进步,但本发明决非仅局限于实施例。Below through specific embodiment, further set forth substantive characteristic and remarkable progress of the present invention, but the present invention is by no means limited to embodiment.
实施例:Example:
现有的连续式熔铝炉每小时熔铝500公斤。过热区安装两台重油燃烧机,油耗每小时20公斤。采用三台30仟瓦电阻炉(每台盛铝水500公斤)同时操作,调整铝液温度至700℃后,用氮气对铝液进行去气处理。经过扒渣、静置后,浇注汽车零件毛坯。此项操作大约进行3小时。每公斤铝合金耗电量在0.20度左右。改成本发明的结构后,可以保证获得合适的铝液温度(见表2),从而取消了电阻炉,每吨铝水节省200度电。The existing continuous aluminum melting furnace melts 500 kilograms of aluminum per hour. Two heavy oil burners are installed in the overheating area, and the fuel consumption is 20 kg per hour. Three 30 kW resistance furnaces (each containing 500 kg of aluminum water) are used to operate simultaneously. After adjusting the temperature of the aluminum liquid to 700 ° C, the aluminum liquid is degassed with nitrogen. After slag removal and standing still, the blanks of auto parts are poured. This operation takes about 3 hours. The power consumption per kilogram of aluminum alloy is about 0.20 degrees. After changing the structure of the present invention, it can guarantee to obtain the suitable temperature of molten aluminum (see Table 2), thereby canceling the resistance furnace, and saving 200 kwh of electricity per ton of molten aluminum.
表2不同部位铝液温度℃Table 2 Temperature of molten aluminum in different parts ℃
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SU1719838A1 (en) * | 1989-07-27 | 1992-03-15 | Пензенский Политехнический Институт | Reverberate shaft furnace for melting aluminum and aluminum alloys |
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CN85201505U (en) * | 1985-05-10 | 1985-09-10 | 颜孟秋 | Quick aluminum melting furnace |
US4832911A (en) * | 1986-09-18 | 1989-05-23 | Alcan International Limited | Method of alloying aluminium |
SU1719838A1 (en) * | 1989-07-27 | 1992-03-15 | Пензенский Политехнический Институт | Reverberate shaft furnace for melting aluminum and aluminum alloys |
WO1999000172A1 (en) * | 1997-06-26 | 1999-01-07 | Asahi Medical Co., Ltd. | Leukapheretic filter medium |
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