CN104032333B - A kind of closing down magnesium electrolysis bath of high current efficiency double collection magnesium room - Google Patents
A kind of closing down magnesium electrolysis bath of high current efficiency double collection magnesium room Download PDFInfo
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- CN104032333B CN104032333B CN201410270112.9A CN201410270112A CN104032333B CN 104032333 B CN104032333 B CN 104032333B CN 201410270112 A CN201410270112 A CN 201410270112A CN 104032333 B CN104032333 B CN 104032333B
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- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 title claims abstract description 89
- 239000011777 magnesium Substances 0.000 title claims abstract description 86
- 229910052749 magnesium Inorganic materials 0.000 title claims abstract description 86
- 238000005868 electrolysis reaction Methods 0.000 title abstract description 14
- 238000000926 separation method Methods 0.000 abstract description 10
- 239000003792 electrolyte Substances 0.000 abstract description 9
- 238000000034 method Methods 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 2
- 229910052751 metal Inorganic materials 0.000 description 14
- 239000002184 metal Substances 0.000 description 14
- 238000010586 diagram Methods 0.000 description 10
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 229910000838 Al alloy Inorganic materials 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 229910000861 Mg alloy Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003562 lightweight material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Electrolytic Production Of Metals (AREA)
Abstract
Description
【技术领域】【Technical field】
本发明涉及电解槽技术领域,具体地说,是一种高电流效率双集镁室的镁电解槽。The invention relates to the technical field of electrolytic cells, in particular to a magnesium electrolytic cell with high current efficiency and double magnesium collecting chambers.
【背景技术】【Background technique】
镁是最轻的有色金属,能够很好的与其它金属构成高强度的合金,且不断改善的可铸性使其应用领域越来越广,是传统铝合金等的有益补充。在美国,镁合金在消费电子、汽车、医疗等领域出现爆发式增长,大有替代铝合金等传统合金之势。镁不仅作为轻量化材料而备受期待,还作为镁燃料电池的电极构造材料,在电池行业有着重要的应用。Magnesium is the lightest non-ferrous metal, which can form high-strength alloys with other metals well, and its continuous improvement of castability makes it more and more widely used, and it is a beneficial supplement to traditional aluminum alloys. In the United States, magnesium alloys have experienced explosive growth in the fields of consumer electronics, automobiles, and medical care, and are likely to replace traditional alloys such as aluminum alloys. Magnesium is not only expected as a lightweight material, but also as an electrode construction material for magnesium fuel cells, which has important applications in the battery industry.
中国是镁资源大国,也是金属镁生产大国,但生产方法主要以皮江法为主。国内电解法生产工艺设备落后、槽型小、电流效率及生产效率低、能耗高。相比之下国外电解设备电流强度大,自动化程度高,单位面积金属镁产量高,电耗低。我国目前运行的无隔板镁电解槽的电流效率低,仅在76~78%左右,金属镁分离效率低,整个镁电解工业与国外差距巨大。China is a country with large magnesium resources and a large producer of magnesium metal, but the production method is mainly Pidgeon method. The domestic electrolysis production process equipment is backward, the cell type is small, the current efficiency and production efficiency are low, and the energy consumption is high. In contrast, foreign electrolysis equipment has high current intensity, high degree of automation, high output of metal magnesium per unit area, and low power consumption. The current efficiency of magnesium electrolyzers without separators currently in operation in my country is only about 76-78%, and the separation efficiency of metal magnesium is low. The entire magnesium electrolysis industry has a huge gap with foreign countries.
基于对先进镁电解工艺的研究,设计出具备低能量消耗、高金属镁分离率的电解槽。同时开发具有我国自主知识产权的镁电解关键技术,进一步与天然气化工有机结合,形成镁、天然气化工等各项资源相互依托、互相支撑的循环经济产业链,达到资源利用的最大化和经济效益的最佳化。Based on the research on the advanced magnesium electrolysis process, an electrolytic cell with low energy consumption and high metal magnesium separation rate is designed. At the same time, develop the key technology of magnesium electrolysis with my country's independent intellectual property rights, and further organically combine with natural gas chemical industry to form a circular economy industrial chain in which various resources such as magnesium and natural gas chemical industry rely on each other and support each other, so as to maximize resource utilization and maximize economic benefits. optimize.
【发明内容】【Content of invention】
本发明的目的在于克服现有技术的不足,提供一种高电流效率双集镁室的镁电解槽。The purpose of the present invention is to overcome the deficiencies of the prior art and provide a magnesium electrolytic cell with high current efficiency and double magnesium collecting chambers.
本发明的目的是通过以下技术方案来实现的:The purpose of the present invention is achieved through the following technical solutions:
一种高电流效率双集镁室的镁电解槽,镁电解槽包含阴极板,阳极板和集镁室,集镁室的数目为两个,分别设置在阴极板和阳极板的两侧,且两个集镁室呈对称分布。A magnesium electrolytic cell with high current efficiency and double magnesium collecting chambers, the magnesium electrolytic cell includes a cathode plate, an anode plate and a magnesium collecting chamber, the number of the magnesium collecting chambers is two, respectively arranged on both sides of the cathode plate and the anode plate, and The two magnesium collecting chambers are distributed symmetrically.
所述的阴极板和阳极板间距为0.03~0.08m。The distance between the cathode plate and the anode plate is 0.03-0.08m.
所述的阴极板从电解槽顶部或者底部插入到镁电解槽中。The cathode plate is inserted into the magnesium electrolytic cell from the top or bottom of the electrolytic cell.
所述的阳极板从电解槽顶部或者底部插入到镁电解槽中。The anode plate is inserted into the magnesium electrolytic cell from the top or bottom of the electrolytic cell.
所述的阴极板和阳极板的宽度和高度相同。The cathode plate and the anode plate have the same width and height.
所述的阴极板和阳极板的宽度的范围为0.9~1.6mThe range of the width of the cathode plate and the anode plate is 0.9~1.6m
所述的阴极板和阳极板的高度的范围为2.0~3.0mThe range of the height of the cathode plate and the anode plate is 2.0~3.0m
所述的阴极板的厚度为0.05~0.15m。The thickness of the cathode plate is 0.05-0.15m.
所述的阳极板的厚度为0.15~0.25m。The thickness of the anode plate is 0.15-0.25m.
与现有技术相比,本发明的积极效果是:Compared with prior art, positive effect of the present invention is:
本发明改变了传统镁电解槽的结构,采用两个对称的集镁室,两个集镁室间采取上插或者下插阴、阳极的方法。该结构改变了镁电解槽的电解质流动情况,充分利用了电解质的流动特性,提高了金属镁的分离效率。与原槽型相比,高效双集镁室电解槽的金属镁分离效率大幅提高,效果明显。The invention changes the structure of the traditional magnesium electrolytic cell, adopts two symmetrical magnesium collecting chambers, and adopts the method of inserting the cathode and the anode upwardly or downwardly between the two magnesium collecting chambers. The structure changes the flow condition of the electrolyte in the magnesium electrolyzer, makes full use of the flow characteristics of the electrolyte, and improves the separation efficiency of metal magnesium. Compared with the original cell type, the metal magnesium separation efficiency of the high-efficiency double magnesium collecting chamber electrolytic cell is greatly improved, and the effect is obvious.
【附图说明】【Description of drawings】
下面结合附图和实施例对本发明进一步说明。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
图1是原型镁电解槽结构示意图;a为外观图,b为横截面示意图Figure 1 is a schematic diagram of the structure of the prototype magnesium electrolytic cell; a is the appearance diagram, b is a cross-sectional schematic diagram
图2是高效双集镁室电解槽结构示意图;a为外观图,b为横截面示意图Figure 2 is a schematic diagram of the high-efficiency dual-magnesium chamber electrolyzer; a is the appearance diagram, and b is a cross-sectional schematic diagram
图3是镁电解槽原槽型流场分布示意图;Fig. 3 is a schematic diagram of the flow field distribution of the original tank type of magnesium electrolyzer;
图4是高效双集镁室电解槽流场分布示意图;Fig. 4 is a schematic diagram of the flow field distribution of the high-efficiency double magnesium collecting chamber electrolyzer;
图5是镁电解槽原槽型金属镁流动示意图;Fig. 5 is the flow schematic diagram of the original tank type metal magnesium of magnesium electrolyzer;
图6是高效双集镁室电解槽金属镁流动示意图;Figure 6 is a schematic diagram of the flow of metal magnesium in an electrolytic cell with high-efficiency double-collecting magnesium chambers;
附图中的标号分别为:1、阳极,2、阴极,3、电解室,4、集镁室The labels in the accompanying drawings are: 1. Anode, 2. Cathode, 3. Electrolysis chamber, 4. Magnesium collection chamber
【具体实施方式】【detailed description】
以下提供本发明一种高电流效率双集镁室的镁电解槽的具体实施方式。The following provides a specific embodiment of a magnesium electrolytic cell with high current efficiency and double magnesium collecting chambers of the present invention.
实施例1Example 1
请参见附图2,一种高效双集镁室电解槽结构基本部件为阳极1、阴极2、电解室3和两个集镁室4。所述的阴极板和阳极板间距为0.07m,阴极和阳极从电解槽顶部插入到镁电解槽中,阴极和阳极的宽度和高度相同,宽度为1m,高度为2.2m,阴极板厚度为0.05m,阳极板厚度为0.15m。Please refer to accompanying drawing 2, the basic components of a high-efficiency double magnesium collection chamber electrolyzer structure are anode 1, cathode 2, electrolysis chamber 3 and two magnesium collection chambers 4. The distance between the cathode plate and the anode plate is 0.07m, the cathode and the anode are inserted into the magnesium electrolytic cell from the top of the electrolytic cell, the width and height of the cathode and the anode are the same, the width is 1m, the height is 2.2m, and the thickness of the cathode plate is 0.05 m, the thickness of the anode plate is 0.15m.
通过电场、热场、磁场、流场分析,上插阴极式镁电解槽热平衡良好,Through the analysis of electric field, thermal field, magnetic field and flow field, the thermal balance of the upward inserted cathode magnesium electrolytic cell is good,
电解质温度为700℃,电解质流动状态良好,金属镁分离率大幅提升。计算得到电解槽流场分布如图4:金属镁的流动情况如图6:The electrolyte temperature is 700°C, the electrolyte flow state is good, and the separation rate of metal magnesium is greatly improved. The calculated flow field distribution of the electrolytic cell is shown in Figure 4; the flow of metal magnesium is shown in Figure 6:
如图可知高效双集镁室电解槽,金属镁随着电解质分别流入左右两个对称的集镁室,并最终在集镁室的电解质液面汇集。几乎没有金属镁存在电解室中,金属镁分离率极高。It can be seen from the figure that in the high-efficiency double magnesium collecting chamber electrolyzer, metal magnesium flows into the left and right symmetrical magnesium collecting chambers respectively with the electrolyte, and finally gathers at the electrolyte liquid level of the magnesium collecting chamber. Almost no metal magnesium exists in the electrolytic chamber, and the separation rate of metal magnesium is extremely high.
对比例1Comparative example 1
请参见附图1,原型镁电解槽结构基本部件阳极1、阴极2、电解室3和集镁室4。Please refer to accompanying drawing 1, the basic components of the prototype magnesium electrolyzer structure anode 1, cathode 2, electrolysis chamber 3 and magnesium collection chamber 4.
与原槽型相比,高效双集镁室电解槽热平衡良好,电解质温度控制在700℃上下,基本工艺参数维持稳定。同时金属镁一次分离率从17%增加至96%,分离效率大幅提高。Compared with the original cell type, the high-efficiency double magnesium collecting chamber electrolytic cell has a good thermal balance, the electrolyte temperature is controlled at around 700°C, and the basic process parameters remain stable. At the same time, the one-time separation rate of magnesium metal increased from 17% to 96%, and the separation efficiency was greatly improved.
以上所述仅是本发明的优选实施方式,应当指出,对于本技术领域的普通技术人员,在不脱离本发明构思的前提下,还可以做出若干改进和润饰,这些改进和润饰也应视为本发明的保护范围内。The above is only a preferred embodiment of the present invention, it should be pointed out that for those of ordinary skill in the art, without departing from the concept of the present invention, some improvements and modifications can also be made, and these improvements and modifications should also be considered Within the protection scope of the present invention.
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SU507669A1 (en) * | 1974-09-06 | 1976-03-25 | Всесоюзный научно-исследовательский и проектный институт алюминиевой, магниевой и электродной промышленности | Electrolyzer to get magnesium |
US4058448A (en) * | 1976-06-23 | 1977-11-15 | Muzhzhavlev Konstantin Dmitrie | Diaphragmless electrolyzer for producing magnesium and chlorine |
CN1807697A (en) * | 2005-12-28 | 2006-07-26 | 中国科学院长春应用化学研究所 | Process for preparing rare earth-magnesium intermediate alloy by compound cathode molten salt electrolysis |
CN200955069Y (en) * | 2006-06-14 | 2007-10-03 | 贵阳铝镁设计研究院 | Magnesium-conducting trough-type magnesium electrolytic cell |
TW201418524A (en) * | 2012-11-05 | 2014-05-16 | Univ Nat Yunlin Sci & Tech | Apparatus and method for electrolytically producing magnesium |
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2014
- 2014-06-17 CN CN201410270112.9A patent/CN104032333B/en active Active
Patent Citations (5)
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SU507669A1 (en) * | 1974-09-06 | 1976-03-25 | Всесоюзный научно-исследовательский и проектный институт алюминиевой, магниевой и электродной промышленности | Electrolyzer to get magnesium |
US4058448A (en) * | 1976-06-23 | 1977-11-15 | Muzhzhavlev Konstantin Dmitrie | Diaphragmless electrolyzer for producing magnesium and chlorine |
CN1807697A (en) * | 2005-12-28 | 2006-07-26 | 中国科学院长春应用化学研究所 | Process for preparing rare earth-magnesium intermediate alloy by compound cathode molten salt electrolysis |
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Non-Patent Citations (2)
Title |
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