Electronic-grade lead titanate purification processing auxiliary equipment

Abstract

The utility model discloses electronic-grade lead titanate purification processing auxiliary equipment which comprises a main material tank, one side of the main material tank is connected with a first liquid conveying pipeline, the output end of the first liquid conveying pipeline is communicated with a liquid mixing device, the first liquid conveying pipeline is communicated with the input end of the liquid mixing device, an auxiliary material tank is further matched with the main material tank, and the auxiliary material tank is communicated with the input end of the liquid mixing device. Main materials in the main material tank are quantitatively output through the first liquid conveying pipeline, meanwhile, the control system adjusts output operation of the second liquid conveying pipeline according to information feedback of the first liquid conveying pipeline, auxiliary materials in the auxiliary material tank are quantitatively guided into the output end of the main liquid pipe, and then the preliminarily mixed materials are subjected to deep wall breaking and mixing fusion through the liquid mixing device; then, the materials are subjected to flowing heating through a flowing industrial water heater to reach the appropriate temperature for reaction, and finally, the materials flow into a heat preservation type storage tank to be subjected to centralized storage and deep reaction; and continuous processing can be carried out according to actual production requirements.

Description

TECHNICAL FIELD

[0001] The utility model relates to the production technology field of lead titanate, specifically to a kind of electronic grade lead titanate purification processing auxiliary equipment. BACKGROUND

[0002] Electronic grade lead titanate is a kind of high-purity lead titanate material, mainly used in electronic field. At present, the proportion of raw materials, reaction conditions (temperature) and impurity control in the purification process need to be mainly noticed when electronic grade lead titanate is purified. However, the existing electronic grade lead titanate purification equipment still has some deficiencies in processing. The current electronic grade lead titanate purification equipment usually stirs, stands and reacts on the quantitative lead titanate material in the form of a separate container tank, so as to obtain the required electronic grade lead titanate stock solution without dehydration. In actual production, the amount of lead titanate purification is generally large. The existing electronic grade lead titanate processing equipment cannot produce continuously, so in order to improve unit output, only the number of equipment can be increased, which not only increases production cost but also affects the production efficiency of enterprise. SUMMARY

[0003] The purpose of this section is to outline some aspects of the embodiments of the utility model and briefly introduce some preferred embodiments. Some simplifications or omissions may be made in this section and the abstract of the specification and the utility model name to avoid obscuring the purpose of this section, the abstract of the specification and the utility model name. Such simplifications or omissions cannot be used to limit the scope of the utility model.

[0004] Therefore, the purpose of the utility model is to provide an electronic grade lead titanate purification processing auxiliary equipment to solve the problem that the existing electronic grade lead titanate processing equipment cannot produce continuously, so in order to improve unit output, only the number of equipment can be increased, which not only increases production cost but also affects the production efficiency of enterprise.

[0005] To achieve the above purpose, the utility model provides the following technical scheme: an electronic grade lead titanate purification processing auxiliary equipment, which comprises a main tank, a first infusion pipeline is connected to one side of the main tank, a mixed liquid device is connected to the output end of the first infusion pipeline, and the first infusion pipeline is connected to the input end of the mixed liquid device. The main tank is matched with an auxiliary tank, the auxiliary tank is connected to one side of the first infusion pipeline through a second infusion pipeline, the output end of the mixed liquid device is connected to an industrial water heater, and the output end of the industrial water heater is connected to a heat preservation type storage tank.

[0006] As a preferred embodiment of the auxiliary equipment for the purification and processing of electronic-grade lead titanate described in this utility model, the first liquid delivery pipeline includes a main liquid pipe with one end connected to the main material tank and the other end connected to the input end of the mixing device, a metering pump I installed on the main liquid pipe, and a float flow meter installed on the main liquid pipe and located in the direction of the output end of the metering pump I.

[0007] As a preferred embodiment of the auxiliary equipment for the purification and processing of electronic-grade lead titanate described in this utility model, the second infusion pipeline includes an auxiliary liquid pipe with one end connected to the auxiliary material tank and the other end connected to the output end of the main liquid pipe, a metering pump II installed on the main liquid pipe, and an electromagnetic flow valve installed at the end of the auxiliary liquid pipe and connected to the main liquid pipe.

[0008] As a preferred embodiment of the auxiliary equipment for the purification and processing of electronic-grade lead titanate described in this utility model, the mixing device is a chemical pipeline mixing pump, and the output port of the chemical pipeline mixing pump also has a drain pipe connected to the input end of an industrial water heater.

[0009] The industrial water heater also has a drain pipe at its output end that connects to an insulated storage tank.

[0010] As a preferred embodiment of the auxiliary equipment for the purification and processing of electronic-grade lead titanate described in this utility model, a drain valve is also provided on one side of the bottom of the insulated storage tank.

[0011] As a preferred embodiment of the auxiliary equipment for the purification and processing of electronic-grade lead titanate described in this utility model, it further includes a base for mounting the equipment and a PLC controller for the main control unit of the equipment.

[0012] Compared with the prior art, the beneficial effects of this utility model are as follows: This auxiliary equipment for the purification and processing of electronic-grade lead titanate quantitatively outputs the main material from the main material tank through the first infusion pipeline. At the same time, the control system adjusts the output operation of the second infusion pipeline based on the information feedback from the first infusion pipeline, and quantitatively introduces the auxiliary material from the auxiliary material tank into the output end of the main liquid pipeline. Then, the material is deeply broken down and stirred and blended by the mixing device after preliminary mixing. Subsequently, the material is heated by the flow of an industrial water heater to reach the appropriate reaction temperature. Finally, it flows into an insulated storage tank for centralized storage and deep reaction. It can continuously process according to the actual production needs without separate batch processing, and the unit output and production efficiency are significantly improved. Attached Figure Description

[0013] Fig. 1 This is a schematic diagram of the overall structure of this utility model;

[0014] Fig. 2 This is a schematic diagram of the infusion pipeline layout structure of this utility model.

[0015] In the figure: 100, main tank; 200, first liquid conveying pipeline; 210, main liquid pipe; 220, metering pump one; 230, float flowmeter; 300, liquid mixing device; 310, liquid discharge pipe; 400, auxiliary tank; 500, second liquid conveying pipeline; 510, auxiliary liquid pipe; 520, metering pump two; 530, electromagnetic flow valve; 600, industrial water heater; 610, dredging pipe; 700, heat preservation type storage tank; 710, liquid discharge valve; 800, base; 900, PLC controller. DETAILED DESCRIPTION

[0016] In order to make the above-mentioned purpose, features and advantages of the present application more apparent, clear and understandable, the specific embodiments of the present application will be described in detail below with reference to the drawings.

[0017] Secondly, the present application is described in detail in combination with the schematic diagram, and in the detailed description of the embodiments of the present application, the cross-sectional view of the device structure will be partially enlarged without the general proportion for the convenience of description, and the schematic diagram is only an example, which should not limit the scope of protection of the present application. In addition, the three-dimensional spatial dimensions of length, width and depth should be included in the actual manufacture.

[0018] In order to make the purpose, technical scheme and advantages of the present application more clear, the embodiments of the present application will be described in further detail below with reference to the drawings.

[0019] Figs. 1-2 The present application is shown as the whole structure schematic diagram of the electronic grade lead titanate purification processing auxiliary equipment, please refer to Figs. 1-2 The electronic grade lead titanate purification processing auxiliary equipment of the present embodiment comprises a main tank 100, a first liquid conveying pipeline 200 is connected to one side of the main tank 100, a liquid mixing device 300 is communicated to the output end of the first liquid conveying pipeline 200, and the first liquid conveying pipeline 200 is communicated to the input end of the liquid mixing device 300. In addition to the main tank 100, there is also an auxiliary tank 400, one side of the auxiliary tank 400 is connected to and communicated to the second liquid conveying pipeline 500 of the first liquid conveying pipeline 200, the output end of the liquid mixing device 300 is communicated to the industrial water heater 600, and the output end of the industrial water heater 600 is communicated to the heat preservation type storage tank 700.

[0020] The first liquid delivery pipeline 200 includes a main liquid pipe 210 having one end connected to the main tank 100 and the other end connected to the input end of the mixing device 300, a metering pump one 220 arranged on the main liquid pipe 210, and a float flowmeter 230 arranged on the main liquid pipe 210 and located in the direction of the output end of the metering pump one 220. The second liquid delivery pipeline 500 includes a secondary liquid pipe 510 having one end connected to the auxiliary tank 400 and the other end connected to the output end of the main liquid pipe 210, a metering pump two 520 arranged on the main liquid pipe 210, and an electromagnetic flow valve 530 arranged at the end of the secondary liquid pipe 510 and connected to the main liquid pipe 210. The cooperation of the metering pump one 220, the float flowmeter 230, the metering pump two 520, and the electromagnetic flow valve 530 ensures the fine output and proportioning of the unit amount of lead titanate main material and auxiliary material. The mixing device 300 is a chemical pipeline mixing pump, and the output port of the chemical pipeline mixing pump also has a liquid discharge pipe 310 connected to the input end of the industrial water heater 600. The output end of the industrial water heater 600 also has a drainage pipe 610 connected to the heat preservation type storage tank 700. The chemical pipeline mixing pump can change the flow state of the fluid in the pipeline, realize uniform mixing between different fluids, has good wall breaking effect, and ensures the rapid fusion of lead titanate materials. In addition, the industrial water heater 600 here also becomes a chemical grade water heater, which has precise unit heat exchange efficiency and can heat the mixed material at constant temperature. Specifically, in the embodiment, the main material in the main tank 100 is quantitatively output through the first liquid delivery pipeline 200, and the control system adjusts the output operation of the second liquid delivery pipeline 500 according to the information feedback of the first liquid delivery pipeline 200, and the auxiliary material in the auxiliary tank 400 is quantitatively introduced into the output end of the main liquid pipe 210. Then, the preliminarily mixed material is subjected to deep wall breaking and mixing and fusion by the mixing device 300, and then the material is subjected to flow heating by the industrial water heater 600 to reach the appropriate temperature for reaction, and finally flows into the heat preservation type storage tank 700 for centralized storage and deep reaction. The actual production needs can be continuously processed without separate batch processing, and the unit production and production efficiency are obviously improved.

[0021] Further, the heat preservation type storage tank 700 also has a liquid discharge valve 710 arranged at one side of the bottom. It can be understood that when the lead titanate material in the heat preservation type storage tank 700 is reacted, the material can be introduced into the lead titanate purification device for concentration and purification through the liquid discharge valve 710. It should be noted that, for the convenience of understanding, the volumes of the heat preservation type storage tank 700, the main tank 100, and the auxiliary tank 400 are relatively small in the figure, and in actual production, such tank bodies can be arranged as large tank bodies or a plurality of connected tank body combinations, which are not limited.

[0022] Furthermore, it also includes a base 800 for mounting the equipment and a PLC controller 900 for the equipment's central control unit. Operators can use the PLC controller 900 to operate the equipment and set data, improving the ease of use of the device.

[0023] Although the present invention has been described above with reference to embodiments, various modifications can be made and components can be replaced with equivalents without departing from the scope of the present invention. In particular, as long as there is no structural conflict, the features in the embodiments disclosed in this invention can be combined with each other in any way. The lack of an exhaustive description of these combinations in this specification is merely for the sake of brevity and resource conservation. Therefore, the present invention is not limited to the specific embodiments disclosed herein, but includes all technical solutions falling within the scope of the claims.

Claims

1. An auxiliary device for the purification and processing of electronic-grade lead titanate, characterized in that, The system includes a main material tank (100), a first infusion pipeline (200) connected to one side of the main material tank (100), a mixing device (300) connected to the output end of the first infusion pipeline (200), and the first infusion pipeline (200) connected to the input end of the mixing device (300). An auxiliary material tank (400) is also connected to the main material tank (100), a second infusion pipeline (500) connected to and connected to the first infusion pipeline (200) on one side of the auxiliary material tank (400). An industrial water heater (600) is connected to the output end of the mixing device (300), and an insulated storage tank (700) is connected to the output end of the industrial water heater (600).

2. The auxiliary equipment for purifying and processing electronic-grade lead titanate according to claim 1, characterized in that: The first infusion pipeline (200) includes a main liquid pipe (210) with one end connected to the main material tank (100) and the other end connected to the input end of the mixing device (300), a metering pump (220) installed on the main liquid pipe (210), and a float flow meter (230) installed on the main liquid pipe (210) and located in the direction of the output end of the metering pump (220).

3. The auxiliary equipment for purifying and processing electronic-grade lead titanate according to claim 1, characterized in that: The second infusion pipeline (500) includes an auxiliary liquid pipe (510) with one end connected to the auxiliary material tank (400) and the other end connected to the output end of the main liquid pipe (210), a metering pump II (520) installed on the main liquid pipe (210), and an electromagnetic flow valve (530) installed at the end of the auxiliary liquid pipe (510) and connected to the main liquid pipe (210).

4. The auxiliary equipment for purifying and processing electronic-grade lead titanate according to claim 1, characterized in that: The mixing device (300) is a chemical pipeline mixing pump, and the output port of the chemical pipeline mixing pump also has a drain pipe (310) connected to the input end of the industrial water heater (600); The industrial water heater (600) also has a drain pipe (610) at its output end that is connected to an insulated storage tank (700).

5. The auxiliary equipment for purifying and processing electronic-grade lead titanate according to claim 1, characterized in that: The insulated storage tank (700) is also equipped with a drain valve (710) on one side of its bottom.

6. The auxiliary equipment for purifying and processing electronic-grade lead titanate according to claim 1, characterized in that: It also includes a base (800) for mounting the equipment, and a PLC controller (900) for the equipment's main control unit.

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