CN103726067B - A kind of electrolysis system producing electrolytic manganese dioxide - Google Patents
A kind of electrolysis system producing electrolytic manganese dioxide Download PDFInfo
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Abstract
本发明涉及一种生产电解二氧化锰的电解系统,其包括电解液预热装置和电解装置,所述电解装置包括槽本体,槽本体中间为隔膜围成的阳极区,在阳极区与槽本体之间区隔为数个阴极区,预热装置内的电解液通过泵输送至每一阴极区,阳极区插有阳极板,每一阴极区插有一阴极板。本发明通过将电解液集中进行预热,然后输送至各个阴极区,使电解装置内的电解液快速电解,提高电解效率;同时,阴极区采用阶梯状槽底,当槽底最深的阴极区通入电解液时,只须启动该区的阴极板电解,依此可实现逐个启动阴极板,从而较低电解成本;本发明还采用导热油加热装置加热,不仅可精确控制加热温度,而且可避免污染电解产品,从而提高产品质量。
The invention relates to an electrolysis system for producing electrolytic manganese dioxide, which includes an electrolyte preheating device and an electrolysis device. The electrolysis device includes a tank body. There are several cathode areas separated between them, and the electrolyte in the preheating device is pumped to each cathode area, an anode plate is inserted in the anode area, and a cathode plate is inserted in each cathode area. In the present invention, the electrolyte is preheated in a concentrated manner, and then transported to each cathode area, so that the electrolyte in the electrolysis device is quickly electrolyzed, and the electrolysis efficiency is improved; at the same time, the cathode area adopts a stepped tank bottom, and when the cathode area with the deepest tank bottom is connected to When entering the electrolyte, it is only necessary to start the electrolysis of the cathode plates in this area, so that the cathode plates can be started one by one, thereby lowering the cost of electrolysis; the invention also uses a heat conduction oil heating device for heating, which can not only accurately control the heating temperature, but also avoid Pollution of electrolytic products, thereby improving product quality.
Description
技术领域technical field
本发明涉及制备电解二氧化锰锰,具体说是生产电解二氧化锰的电解系统。The invention relates to the preparation of electrolytic manganese dioxide manganese, in particular to an electrolytic system for producing electrolytic manganese dioxide.
背景技术Background technique
目前,电解二氧化锰纯度高、晶型好、放电容量大、活性强,是优良的电池去极化剂,由于其具有良好的放电性能,因而成为电池工业的一种非常重要的原料。现有的电解二氧化锰(EMD)生产方法多采用的是H2SO4-MnSO4电解工艺。该电解工艺通常是以铅、铅基合金、石墨或纯钛、钛合金、贵金属氧化物涂层等为阳极,以石墨棒或不锈钢等为阴极,使用硫酸锰溶液作为电解液,通以大电流低压直流电使二价锰离子在阳极上失去电子(发生氧化反应)并最终析出二氧化锰。沉积在阳极上的二氧化锰粗产品经过剥离、粉碎、漂洗、中和、干燥等处理后,即得到电解二氧化锰成品。At present, electrolytic manganese dioxide has high purity, good crystal form, large discharge capacity and strong activity. It is an excellent battery depolarizer. Because of its good discharge performance, it has become a very important raw material for the battery industry. The existing electrolytic manganese dioxide (EMD) production methods mostly use the H2SO4-MnSO4 electrolysis process. The electrolysis process usually uses lead, lead-based alloys, graphite or pure titanium, titanium alloys, noble metal oxide coatings, etc. as the anode, graphite rods or stainless steel as the cathode, and manganese sulfate solution as the electrolyte. Low-voltage direct current causes divalent manganese ions to lose electrons on the anode (oxidation reaction occurs) and finally precipitates manganese dioxide. The crude manganese dioxide deposited on the anode is stripped, pulverized, rinsed, neutralized and dried to obtain the finished electrolytic manganese dioxide.
出于降低生产设备成本、简化生产工艺、提高电解二氧化锰产品质量、提升电解效率考虑,电解过程中往往还需要对电解液进行加热。常用的电解液加热方法是在电解槽中设置电解液加热管,在电解过程中通入110~150℃的饱和蒸汽,通过电解液加热管的换热使电解液的温度保持在设定的范围。基于金属铜的良好导热特性,所述电解液加热管通常会考虑采用铜管,然而,由于电解液中含有的高浓度硫酸在高温条件下会加速铜的溶解,容易造成铜加热管被腐蚀损坏;更重要的是,如果铜进入电解液中,极可能被电解二氧化锰吸附而造成产品污染,进而降低产品品质。In order to reduce the cost of production equipment, simplify the production process, improve the quality of electrolytic manganese dioxide products, and improve the efficiency of electrolysis, it is often necessary to heat the electrolyte during the electrolysis process. The commonly used electrolyte heating method is to install an electrolyte heating tube in the electrolytic cell, and pass in saturated steam at 110-150°C during the electrolysis process, and keep the temperature of the electrolyte within the set range through the heat exchange of the electrolyte heating tube. . Based on the good thermal conductivity of metal copper, copper pipes are usually considered for the electrolyte heating pipe. However, due to the high concentration of sulfuric acid contained in the electrolyte, the dissolution of copper will be accelerated under high temperature conditions, which will easily cause the copper heating pipe to be corroded and damaged. ; More importantly, if copper enters the electrolyte, it is likely to be adsorbed by electrolytic manganese dioxide to cause product pollution, thereby reducing product quality.
发明内容Contents of the invention
针对上述现有技术的缺点,本发明提供一种可精确控制加热温度、成本较低、生产的产品质量较高的生产电解二氧化锰的电解系统。Aiming at the above-mentioned shortcomings of the prior art, the present invention provides an electrolysis system for producing electrolytic manganese dioxide that can precisely control the heating temperature, has low cost, and produces high-quality products.
本发明解决上述技术问题采用以下技术方案:一种生产电解二氧化锰的电解系统,包括电解液预热装置和电解装置,所述电解装置包括槽本体,槽本体中间为隔膜围成的阳极区,在阳极区与槽本体之间区隔为数个阴极区,预热装置内的电解液通过泵输送至每一阴极区,阳极区插有阳极板,每一阴极区插有一阴极板。The present invention adopts the following technical solutions to solve the above technical problems: an electrolysis system for producing electrolytic manganese dioxide, including an electrolyte preheating device and an electrolysis device, the electrolysis device includes a tank body, and the middle of the tank body is an anode area surrounded by a diaphragm , Between the anode area and the tank body, there are several cathode areas. The electrolyte in the preheating device is pumped to each cathode area. An anode plate is inserted in the anode area, and a cathode plate is inserted in each cathode area.
进一步地,所述阳极区与槽本体之间的槽底呈阶梯状,每一阶梯的阶梯面为一阴极区的底面。Further, the bottom of the tank between the anode region and the tank body is stepped, and the step surface of each step is the bottom surface of a cathode region.
作为优选,所述预热装置为一容器,容器器壁上设有数个出液管,每一出液管与一所述阴极区连通,每一出液管上安装有一所述泵。Preferably, the preheating device is a container, and several liquid outlet pipes are arranged on the wall of the container, each liquid outlet pipe communicates with one of the cathode regions, and each liquid outlet pipe is equipped with a said pump.
作为优选,所述容器器壁和槽本体内均设有夹层,夹层内安装有导热油管,导热油管的温度由导热油加热装置控制。Preferably, the container wall and the tank body are provided with an interlayer, and a heat-conducting oil pipe is installed in the interlayer, and the temperature of the heat-conducting oil pipe is controlled by a heat-conducting oil heating device.
作为优选,所述槽底设有废液排出口。Preferably, a waste liquid outlet is provided at the bottom of the tank.
作为优选,所述出液管上设有保温层。Preferably, an insulating layer is provided on the liquid outlet pipe.
本发明与现有技术相比具有如下优点:Compared with the prior art, the present invention has the following advantages:
1、本发明通过将电解液集中进行预热,然后输送至各个阴极区,使电解装置内的电解液快速电解,提高电解效率;1. In the present invention, the electrolyte is preheated in a concentrated manner, and then transported to each cathode area, so that the electrolyte in the electrolysis device is quickly electrolyzed, and the electrolysis efficiency is improved;
2、阴极区采用阶梯状槽底,当槽底最深的阴极区通入电解液时,只须启动该区的阴极板电解,依此可实现逐个启动阴极板,从而较低电解成本;2. The cathode area adopts a stepped tank bottom. When the electrolyte is introduced into the deepest cathode area at the bottom of the tank, it is only necessary to start the electrolysis of the cathode plates in this area, so that the cathode plates can be started one by one, thereby reducing the cost of electrolysis;
3、本发明采用导热油加热装置加热,不仅可精确控制加热温度,而且可避免污染电解产品,从而提高产品质量。3. The present invention adopts a heat conduction oil heating device for heating, which not only can accurately control the heating temperature, but also avoids polluting the electrolytic product, thereby improving product quality.
附图说明Description of drawings
图1是本发明的结构示意图;Fig. 1 is a structural representation of the present invention;
图2是本发明中预热装置的剖视示意图;Fig. 2 is the sectional schematic view of preheating device among the present invention;
图3是本发明中电解装置的俯视示意图。Fig. 3 is a schematic top view of the electrolysis device in the present invention.
具体实施方式detailed description
下面结合图1、图2和图3详细说明本发明:Below in conjunction with Fig. 1, Fig. 2 and Fig. 3 describe the present invention in detail:
本发明的电解系统包括电解液预热装置1和电解装置2,所述电解装置包括槽本体21,槽本体中间为隔膜3围成的阳极区22,在阳极区与槽本体之间区隔为数个阴极区23,预热装置1内的电解液通过泵4输送至每一阴极区,阳极区插有阳极板24,每一阴极区插有一阴极板25。通过预热装置可对电解液进行集中预热,然后输送至各个阴极区,一旦电解液到达电解装置内,即可进行快速电解,提高电解效率。The electrolysis system of the present invention includes an electrolyte preheating device 1 and an electrolysis device 2, the electrolysis device includes a tank body 21, the middle of the tank body is an anode area 22 surrounded by a diaphragm 3, and the anode area and the tank body are separated by several Each cathode area 23, the electrolytic solution in the preheating device 1 is transported to each cathode area by a pump 4, an anode plate 24 is inserted in the anode area, and a cathode plate 25 is inserted in each cathode area. The electrolyte can be preheated intensively through the preheating device, and then transported to each cathode area. Once the electrolyte reaches the electrolysis device, rapid electrolysis can be performed to improve the electrolysis efficiency.
作为本发明另一目的,所述阳极区与槽本体之间的槽底呈阶梯状,每一阶梯的阶梯面为一阴极区的底面。在电解过程中,当电解溶液较少时,可首先向当槽底最深的阴极区通入电解液,只须启动该区的阴极板电解;当电解液的液面逐渐上升后,会逐个淹没其它阴极区的底面,此时逐个启动其它阴极区的阴极板,同时可逐个向启动的阴极区输送电解液。此种设计可根据电解液的多少合理控制电解过程,从而避免了一些不必要的浪费,较低了电解成本。As another object of the present invention, the tank bottom between the anode region and the tank body is stepped, and the step surface of each step is the bottom surface of a cathode region. During the electrolysis process, when there is less electrolytic solution, the electrolyte can be introduced into the deepest cathode area at the bottom of the tank first, and only the cathode plate in this area needs to be electrolyzed; when the liquid level of the electrolyte rises gradually, it will be submerged one by one On the bottom surface of other cathode regions, the cathode plates of other cathode regions are activated one by one at this time, and electrolyte solution can be delivered to the activated cathode regions one by one at the same time. This design can reasonably control the electrolysis process according to the amount of electrolyte, thereby avoiding some unnecessary waste and lowering the cost of electrolysis.
作为优选,所述预热装置1为一容器11,容器器壁上设有数个出液管12,每一出液管与一所述阴极区连通,每一出液管上安装有所述泵4,可精确控制电解液的流量,以控制电解液的补充量,从而达到适时、快速补充电解液的目的。作为优选,所述出液管上设有保温层13,防止热量散失,达到保温效果。As preferably, the preheating device 1 is a container 11, and several liquid outlet pipes 12 are arranged on the wall of the container, and each liquid outlet pipe communicates with one of the cathode regions, and the pump is installed on each liquid outlet pipe. 4. The flow rate of the electrolyte can be precisely controlled to control the replenishment of the electrolyte, so as to achieve the purpose of timely and rapid replenishment of the electrolyte. As a preference, an insulation layer 13 is provided on the outlet pipe to prevent heat loss and achieve an insulation effect.
在本发明中,所述容器器壁和槽本体内均设有夹层5,夹层内安装有导热油管6,导热油管的温度由导热油加热装置7控制,不仅可精确控制加热温度,而且可避免污染电解产品,从而提高产品质量。作为优选,所述槽底设有废液排出口8,可将废液回收利用。In the present invention, the container wall and the tank body are provided with an interlayer 5, and a heat-conducting oil pipe 6 is installed in the interlayer. The temperature of the heat-conducting oil pipe is controlled by a heat-conducting oil heating device 7, which not only can accurately control the heating temperature, but also can avoid Pollution of electrolytic products, thereby improving product quality. Preferably, the bottom of the tank is provided with a waste liquid outlet 8, which can recycle the waste liquid.
以上显示和描述了本发明的基本原理和主要特征及本发明的优点,本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内,本发明要求保护范围由所附的权利要求书及其等效物界定。Above shows and described basic principle of the present invention and main feature and the advantage of the present invention, those skilled in the art should understand that, the present invention is not limited by above-mentioned embodiment, what described in above-mentioned embodiment and description just illustrates the present invention Principle, under the premise of not departing from the spirit and scope of the present invention, the present invention also has various changes and improvements, and these changes and improvements all fall within the claimed scope of the present invention, and the claimed protection scope of the present invention is defined by the appended claims Requirements and their equivalents are defined.
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Publication number | Priority date | Publication date | Assignee | Title |
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US3455811A (en) * | 1966-05-11 | 1969-07-15 | Knapsack Ag | Electrode system for use in the electrolytic production of manganese dioxide |
CN202766628U (en) * | 2012-09-21 | 2013-03-06 | 广西埃赫曼康密劳化工有限公司 | Electrolysis bath for production of electrolyte manganese dioxide |
CN103114300A (en) * | 2012-12-13 | 2013-05-22 | 苏州新区化工节能设备厂 | Single-anode double-cathode ion-exchange membrane electrolytic unit cell |
CN203065589U (en) * | 2012-12-13 | 2013-07-17 | 苏州新区化工节能设备厂 | Single-anode two-cathode ionic membrane electrolytic unit bath |
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US3455811A (en) * | 1966-05-11 | 1969-07-15 | Knapsack Ag | Electrode system for use in the electrolytic production of manganese dioxide |
CN202766628U (en) * | 2012-09-21 | 2013-03-06 | 广西埃赫曼康密劳化工有限公司 | Electrolysis bath for production of electrolyte manganese dioxide |
CN103114300A (en) * | 2012-12-13 | 2013-05-22 | 苏州新区化工节能设备厂 | Single-anode double-cathode ion-exchange membrane electrolytic unit cell |
CN203065589U (en) * | 2012-12-13 | 2013-07-17 | 苏州新区化工节能设备厂 | Single-anode two-cathode ionic membrane electrolytic unit bath |
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