WO2018041059A1 - 一种基于改进型的全自动次氯酸钠发生器系统及实现方法 - Google Patents

一种基于改进型的全自动次氯酸钠发生器系统及实现方法 Download PDF

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WO2018041059A1
WO2018041059A1 PCT/CN2017/099220 CN2017099220W WO2018041059A1 WO 2018041059 A1 WO2018041059 A1 WO 2018041059A1 CN 2017099220 W CN2017099220 W CN 2017099220W WO 2018041059 A1 WO2018041059 A1 WO 2018041059A1
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sodium hypochlorite
hypochlorite generator
brine
automatic
salt
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PCT/CN2017/099220
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English (en)
French (fr)
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刘泽山
闫冠宇
张汉松
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江苏永冠给排水设备有限公司
中国灌溉排水发展中心
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Publication of WO2018041059A1 publication Critical patent/WO2018041059A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00—Electrolytic production of inorganic compounds or non-metals
    • C25B1/01—Products
    • C25B1/24—Halogens or compounds thereof
    • C25B1/26—Chlorine; Compounds thereof
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B15/00—Operating or servicing cells
    • C25B15/02—Process control or regulation

Definitions

  • the invention belongs to the technical field of domestic water treatment equipment, and particularly relates to an improved automatic sodium hypochlorite generator system and an implementation method thereof.
  • the well-known automatic sodium hypochlorite generator system is a domestic water treatment device which is widely used in the technical field of domestic water treatment equipment.
  • the fully automatic sodium hypochlorite generator system has many advantages compared with similar products, the unit design of the salt-dissolving device, the automatic proportioning device, the electrolysis device and the PLC console is not reasonable enough, the configuration is not optimized, and the operating efficiency is The problem of not high, especially the operating system built by the PLC console, can not be connected to the external network for monitoring operation, making the system's practicality and cost performance challenged by the development needs of the high-end market.
  • the electrolytic device In the preparation process of sodium hypochlorite, the electrolytic device is limited by the conditions of the hard water source, so that the electrode surface of the electrolytic cell of the sodium hypochlorite generator device is fouled and attached, and the electrolysis efficiency thereof is remarkably lowered.
  • the pre-electrolysis pre-fabricated softened water anti-fouling, the electrode depolarization descaling, the cooling and anti-scaling of the electrolyzer, and the use of ultrasonic foaming and scaling are often used to solve the problem of effectively preventing electrode surface fouling. problem.
  • 201511033467.7 discloses "an electro-chemical sterilization water processor", It can realize the positive and negative electrode switching after the reaction cell has a certain reaction time, and the electrode instantaneously increases the current to remove the scale fouling on the cathode, but the electrode damage is large, the life of the electrode is greatly shortened, and the real-time shutdown processing is required. It affects the continuous operation of the electrolytic cell and reduces the operating efficiency of the electrolytic cell.
  • Chinese patent application 201120289631.1 discloses an "integrated automatic drinking water disinfection device", which is mainly composed of a rectifier control cabinet, a softener, a salt solution tank, a brine pump, an electrolysis generator, a sodium hypochlorite tank and a dosing pump, Achieve automatic continuous work, economic and practical purposes.
  • Chinese patent application 201520262103.5 discloses a "automatic static sodium hypochlorite generator", including a rectifier, a salt solution tank, a water softener, an electrolysis tank, a storage tank, a tap water inlet pipe, a hydrogen pipe, a brine dosing pump, and a sodium hypochlorite dope.
  • the object of the present invention is to provide an improved automatic sodium hypochlorite generator system and an implementation method thereof, which overcomes the deficiencies of the prior art, and the present invention adopts a networked user station terminal and an improved salt-dissolving device and automatic matching.
  • the unit equipment of the operation and operation of the internal network is greatly optimized, and the operation and monitoring management of the network with the external network is satisfied, thereby significantly improving the operation efficiency of the automatic sodium hypochlorite generator system.
  • a fully automatic sodium hypochlorite generator system based on the improved invention comprises a salt dissolving device, an automatic proportioning device, an electrolyzing device and a dosing device, wherein the functional devices are connected in series in series, and each functional device is provided with control
  • the unit is connected to the PLC console signal through the data line, and is characterized in that it further comprises a networked user station terminal, and the networked user station terminal passes the data line and the PLC console letter.
  • the salt-dissolving device comprises a step-type salt-dissolving device
  • the automatic proportioning device comprises a liquid constant-flow controller
  • the electrolyzing device comprises an integrated anti-scaling electrolyzing device ,among them:
  • the networked user station terminal comprises a data processor and a signal conversion module, a wireless data communication module, a state data acquisition module of the sodium hypochlorite generator device, a self-service program data module of the sodium hypochlorite generator device, and a fault operation program data module.
  • the signal conversion module includes an analog to digital conversion module and a digital mode for converting input and output signals of the networked user station terminal Conversion module.
  • the step-type salt-dissolving device comprises a water inlet, a liquid outlet, a bucket lid, a barrel body, a bucket bottom, a water spray pipe and a stepped salt tank structure, wherein the water spray pipe is connected with the water inlet and fixed to the barrel body
  • the upper part of the spray pipe is provided with a uniformly distributed spray hole
  • the stepped salt tank structure comprises a first layer salt tank and a bottom salt tank, the first layer salt tank is an annular groove structure, and the barrel body and the first layer salt
  • the trough is a unitary structure;
  • the bottom salt trough is a circular structure, and the bottom of the tank is integrated with the bottom salt trough; between the bottom salt trough and the barrel is a saturated brine tank, and the saturated brine tank is connected with the liquid outlet;
  • the liquid constant current controller includes an upper valve body, a lower valve body, an elastic pad and a valve core, the upper valve body is provided with an internal thread, and the lower valve body is provided with an external thread matched with the upper valve body, The upper valve body and the lower valve body are connected by internal and external threads and form a valve body cavity formed by combining the upper valve body and the lower valve body, and the valve body cavity is sequentially disposed along the axial direction of the upper valve body to the lower valve body.
  • the movable valve core comprising a semicircular seal portion and a cylindrical guide portion, the outer surface of the semicircular seal portion being provided with a protrusion, the cylindrical shape a valve core through hole through which a liquid can flow is disposed on a circumferential wall of the guiding portion, and the holed elastic pad is provided with a sealing surface that is matched with the semicircular sealing portion;
  • the integrated anti-fouling electrolysis device comprises a clean brine tank connected to a zoned electrolysis group through a liquid overflow pump with a liquid supply pipe;
  • the clean brine kettle comprises a brine heating kettle with a heater and a belt filter
  • the hot brine filter of the clear material is adjacent to each other, the temperature of the brine in the clean brine heating kettle is 50-100 ° C;
  • the power of the liquid overflow pump is 10-100 w, and the lift is 25-35 m;
  • the electrolysis group comprises 2 to N electrolyzers, wherein each electrolyzer is connected by a liquid increasing pipe; each electrolyzer is provided with a single pair of electrodes including an anode plate and a cathode plate, the single pair The electrode is connected to a DC power source external to the electrolyzer; the flow rate of the electrolyte in the compartmental electrolysis group is not less than the water flow rate of the brine in the clean brine tank.
  • the realization principle of the invention is that the improved automatic sodium hypochlorite generator system and the implementation method proposed by the invention are a comprehensive technical improvement of the existing traditional automatic sodium hypochlorite generator system, specifically: preparing saturated brine
  • the salt-dissolving device is a step-type salt-dissolving device, which can utilize the kinetic energy and potential energy of the water itself to repeatedly impact the salt in the mixed salt silo from a high place, and thoroughly mix the salt with the water; the liquid constant flow control is adopted in the automatic proportioning device.
  • the cross section of the liquid flow path can be inversely proportional to the change of the liquid pressure, thereby ensuring the liquid flow rate is constant;
  • the electrolysis device is an integrated anti-fouling electrolysis device, pre-fabricated clean high-temperature brine, increasing liquid before electrolysis
  • a new scheme of flow velocity and multi-pot electrolysis which integrates measures of descaling, anti-scaling and scale inhibition, and plays a role in synergistic anti-fouling;
  • networked user station terminal and PLC console Collaborative construction can not only perform intranet operation with various functional units of the system, but also operate monitoring and management with the external network, which not only greatly optimizes intranet operation. Unit operation of equipment, but also to meet the needs of network operation and external network monitoring and management.
  • the present invention is directed to an existing well-known salt-dissolving device, automatic proportioning device, electrolyzing device, and PLC control device, and the like, which also has an improvement in design, such as unreasonable design, insufficient configuration, and low operational efficiency.
  • the type of automatic sodium hypochlorite generator system, and each unit device plays a good synergistic effect, so the utility model and the cost performance of the invention are significantly improved, and can meet the needs of the development of the high-end market in the field.
  • the integrated anti-fouling sodium hypochlorite generator device constructed by the invention exerts a good integrated division by adopting measures such as pre-preparing clean brine, increasing liquid flow rate and multi-pot electrolysis before electrolysis.
  • measures such as pre-preparing clean brine, increasing liquid flow rate and multi-pot electrolysis before electrolysis.
  • the synergistic effect of scale, anti-scaling and scale inhibition has achieved more significant effects than the anti-fouling measures of the prior art.
  • the salt-dissolving device for preparing saturated brine constructed by the invention is a step-type salt tank device, which can utilize the kinetic energy and potential energy of the water itself to repeatedly impact the salt in the mixed salt silo from a high place to ensure the salt and water are thoroughly mixed and improved. The efficiency of saturated brine formulation.
  • the liquid flow constant control device for the automatic proportioning device constructed by the invention can make the cross section of the liquid flow channel change inversely with the change of the liquid pressure, thereby ensuring that the liquid flow rate is constant and satisfying the accurate measurement. Need.
  • the networked user station terminal constructed by the invention can perform internal network operation operation through the PLC console and various functional unit devices of the system, and can also operate monitoring management with the external network, greatly improving the improvement. Operational reliability and performance of a fully automatic sodium hypochlorite generator system.
  • FIG. 1 is a block diagram showing the structure of an internal network based on a modified automatic sodium hypochlorite generator system according to the present invention.
  • FIG. 2 is a block diagram showing the structure of an internal network and an external network based on an improved automatic sodium hypochlorite generator system according to the present invention.
  • FIG. 3 is a schematic cross-sectional structural view of a step type salt-dissolving device proposed by the present invention.
  • FIG. 4 is a schematic block diagram showing the structure of a networked user station terminal according to the present invention.
  • FIG. 5 is a schematic structural view of a liquid constant current controller according to the present invention
  • FIG. 5 includes FIG. 5-1, FIG. 5-2, FIG. 5-3, FIG. 5-4, FIG. 5-5, FIG. 5-6, and FIG. 5-7
  • Figure 5-1 is a schematic view of the three-dimensional structure
  • Figure 5-2 is a schematic view of the overall cross-sectional structure
  • Figure 5-3 is a schematic view of the cavity structure of the valve body
  • Figure 5-4 is a schematic view of the three-dimensional structure of the elastic pad
  • Figure 5-5 is a schematic cross-sectional structural view of the elastic pad
  • Figure 5-6 is a schematic perspective view of the movable valve core
  • Figure 5-7 is a schematic cross-sectional structural view of the movable valve core.
  • Fig. 6 is a schematic view showing the vertical structure of the integrated anti-fouling electrolysis device according to the present invention.
  • Fig. 7 is a schematic view showing the horizontal structure of the integrated anti-fouling electrolysis device according to the present invention.
  • FIG. 8 is a schematic block diagram showing the implementation of a modified automatic sodium hypochlorite generator system according to the present invention.
  • a modified automatic sodium hypochlorite generator system according to the present invention comprises a salt-dissolving device (1), an automatic proportioning device (2), an electrolysis device (3) and a dosing device (4), Each functional device is connected in series through a connecting pipe (5), and each functional device is provided with a control unit and is respectively connected with a PLC console (7) through a data line (6), which is characterized in that it also includes a networked user station.
  • the salt device (1) comprises a stepped salt dissolving device, an automatic proportioning device (2) comprising a liquid constant current controller, and an electrolysis device (3) comprising an integrated anti-fouling electrolysis device.
  • the external network monitoring system comprises a background cloud server, a wireless data communication network and an intelligent remote group control self-service server, and the wireless data communication network and the background cloud respectively
  • the server and the intelligent remote group control self-service server perform data communication connection;
  • the back-end cloud server supports the intelligent group control self-service server and the networked user station terminal to perform interactive data communication through the wireless data communication network. Therefore, the present invention can perform intranet operation only through the networked user station terminal (8) and each functional unit of the system, and the invention can also be operated and monitored by the networked user station terminal (8) and the external network.
  • the networked user station terminal (8) of the present invention includes data processor and signal conversion module, wireless data communication module, state data acquisition module of sodium hypochlorite generator device, self-service program data of sodium hypochlorite generator device. a module, a faulty operation program data module and a video and audio prompter signal connection, and a power management module for powering the networked user station terminal;
  • the signal conversion module includes means for converting the input and output of the networked user station terminal The analog to digital conversion module and the digital to analog conversion module of the signal.
  • the step type salt-dissolving device of the present invention comprises a water inlet (1-1), a liquid outlet (1-2), a barrel cover (1-3), a barrel body (1-4), and a bottom of the barrel.
  • (1-5) water spray pipe (1-6) and stepped salt tank structure, the water spray pipe (1-6) is connected to the water inlet (1-1), and is fixed to the barrel body (1-4)
  • the upper part of the spray pipe (1-6) is provided with a uniformly distributed spray hole;
  • the stepped salt tank structure comprises a first layer salt tank (1-7.1) and a bottom salt tank (1-7.2)
  • the first layer salt tank (1-7.1) is an annular groove structure, the barrel body (1-4) is integrated with the first layer salt tank (1-7.1); the bottom salt tank (1-7.2) is a circular structure, the barrel
  • the bottom (1-5) is integrated with the bottom salt tank (1-7.2); between the bottom salt tank (1-7.2) and the barrel (1-4) is a saturated brine tank, a saturated brine tank and a liquid outlet.
  • a preferred embodiment thereof further includes an intermediate layer salt tank (1-7.3) having an annular structure between the first layer salt tank (1-7.1) and the bottom salt tank (1-7.2), the intermediate layer salt tank (1) -7.3) The width of the notch is gradually widened from the first salt bath (1-7.1) to the intermediate salt tank (1-7.3) to form a stepped structure, and the intermediate salt tank (1-7.3) is set to one.
  • the layer or layers, the barrel body (4) and the intermediate layer salt tank (1-7.3) are integrated.
  • the liquid constant current controller of the present invention comprises an upper valve body (2-1), a lower valve body (2-2), an elastic pad (2-3) and a movable valve core (2-4).
  • the upper valve body (2-1) is provided with an internal thread (2-1.1)
  • the lower valve body (2-2) is provided with an external thread that cooperates with the upper valve body (2-1) (2-2.1), the upper valve body (2-1) and the lower valve body (2-2) are connected by internal and external threads and form a valve combining the upper valve body (2-1) and the lower valve body (2-2)
  • the body cavity (2-5), in the valve body cavity (2-5), has a hole-like elasticity sequentially along the axial direction of the upper valve body (2-1) to the lower valve body (2-2)
  • Pad (2-3) and movable spool (2-4) the movable spool (2-4) comprising a semi-circular seal (2-4.1) and a cylindrical guide ( 2-4.2), the outer surface of the semicircular sealing portion (2-4.1) is provided with a projection (2-4.4
  • the gap between the cylindrical guide portion (2-4.2) and the lower valve body (2-2) is provided with a gap (2-6) for liquid circulation, and the gap (2-6) Width is 0.2-5 mm;
  • the shape of the protrusion (2-4.4) is hemispherical, the height of the protrusion (2-4.4) is 0.2-5 mm;
  • the valve body (2-2) is made of stainless steel, copper alloy, aluminum alloy or engineering plastic;
  • the perforated elastic pad (2-3) is made of rubber, silicone or silicone rubber;
  • the material of (2-4) is ceramic or engineering plastic.
  • the integrated anti-fouling electrolysis apparatus of the present invention comprises a clean brine tank through a liquid flow-increasing pump (3-5) with a liquid delivery tube (3-6) and a compartmentalized electrolysis.
  • the clean brine kettle comprises a brine heating kettle (3-1) with a heater (3-3) and a hot brine filter with a filter material (3-4) (3- 2) adjoining, the temperature of the brine in the clean brine heating kettle (3-1) is 50-100 ° C; the power of the liquid overflow pump (3-5) is 10-100 w, the lift is 25-35 m;
  • the compartmental electrolysis group (3-9) comprises 2 to N electrolyzers, wherein each electrolyzer is connected by a liquid-increasing tube (3-8); each of the electrolyzers is provided with an anode pole a single pair of electrodes (3-7) of the plate and the cathode plate, the single pair of electrodes (3-7) being connected to a DC power source external to the electro
  • the heater (3-3) of the brine heating kettle (3-1) is disposed inside the brine heating kettle (3-1) or outside the brine heating kettle (3-1);
  • the brine temperature in the brine heating kettle (3-1) is 70 ° C;
  • the filtration material (3-4) of the hot brine filtration tank (3-2) is a natural zeolite or an ion exchange resin;
  • the liquid-increasing pump (3-5) in the scaled electrolysis equipment has an electric power of 40 W and a head of 30 m; the water flow velocity of the hot brine in the clean brine tank and the electrolysis in the compartmental electrolysis group (3-9)
  • the liquid flow rate of the liquid is not less than 1 m / sec;
  • the diameter of the nozzle of the liquid overflow pipe (3-8) is a liquid transfer pipe (3-6)
  • the diameter of the nozzle is 1/2 to 3/4.
  • Example 6 Referring to FIG. 8, a method for implementing an improved automatic sodium hypochlorite generator system based on the improved method includes the following specific steps:
  • Step 1 boot network control: the user's automatic sodium hypochlorite generator equipment is ready for operation.
  • the user opens the user equipment login account of the networked user station terminal (8), inputs the startup information of the corresponding user terminal, and instructs the PLC console to dissolve.
  • the internal network operation control system constructed by each control unit of the salt device (1), the automatic proportioning device (2), the electrolysis device (3) and the dosing device (4) enters an activation state; at the same time, the networked user station terminal (8)
  • the startup information of the corresponding client is reported to the external network monitoring system (9) and the receiving of the feedback command is completed until the automatic sodium hypochlorite generator device of the user terminal is successfully connected to the network and enters the running state;
  • Step 2 Network operation control: After the user-automatic sodium hypochlorite generator device is successfully connected to the network and enters the running state, the salt-dissolving device (1), the automatic proportioning device (2), the electrolysis device (3) and the investment Each control unit of the adding device (4) respectively receives the command sent by the PLC console (7) and implements the control of each functional unit, and at the same time, the networked user station terminal (8) integrates the internal operation of the PLC console (7). The operation control information of the control system is reported to the external network monitoring system (9) for backup;
  • Step 3 Networking troubleshooting control: In the networked operation control in step 2, if the automatic sodium hypochlorite generator device corresponding to the user terminal is in an abnormal state, the external network monitoring system will be based on the corresponding user terminal networked user station terminal (8) The reported operation control information gives an information prompt for instructing the networked user station terminal (8) to perform the troubleshooting operation until the automatic sodium hypochlorite generator device corresponding to the user terminal is changed from the operation abnormality to the normal operation, and the networked user station terminal ( 8) Reporting the troubleshooting information to the external network monitoring system (9) for backup;
  • Step 4 Shutdown networking control:
  • the networked user station terminal (8) reports the shutdown and shutdown information of the fully automatic sodium hypochlorite generator device corresponding to the user terminal to the external network.
  • the monitoring system (9), the external network monitoring system (9) according to the reported shutdown and shutdown information, the corresponding user terminal networked user station terminal (8) shutdown and subsequent cleaning operation procedures for the automatic sodium hypochlorite generator device
  • the information prompts until the automatic sodium hypochlorite generator device corresponding to the user end completes the cleaning operation procedure and reports the cleaning operation information to the external network monitoring system (9), so as to backup the automatic sodium hypochlorite generator device corresponding to the user end has entered the state of stopping operation.
  • the invention has been verified by trial and error and has achieved satisfactory trial results.

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Abstract

一种基于改进型的全自动次氯酸钠发生器系统及实现方法，系统包括溶盐装置（1）、自动配比装置（2）、电解装置（3）和投加装置（4），各功能装置依次串联连接，各功能装置中均设有控制单元并分别通过数据线（6）与PLC控制台（7）信号连接，还包括联网用户工位终端（8），联网用户工位终端（8）通过数据线与PLC控制台（7）信号连接，还与外网监控系统（9）进行交互式无线数据通信；溶盐装置（1）包括阶梯式溶盐设备，自动配比装置（2）包括液体恒流控制器、电解装置（3）包括集成式防结垢的电解设备。

Description

一种基于改进型的全自动次氯酸钠发生器系统及实现方法 技术领域
本发明属于生活用水处理设备技术领域，特别是涉及一种基于改进型的全自动次氯酸钠发生器系统及实现方法。
背景技术
目前，公知的全自动次氯酸钠发生器系统是生活用水处理设备技术领域中应用面广量大的生活用水处理设备。虽然全自动的次氯酸钠发生器系统与同类产品相比有许多优点，但因溶盐装置、自动配比装置、电解装置和PLC控制台等各单元装置还存在设计不够合理、配置不够优化和运行效率不高等问题，特别是由PLC控制台构建的内网运行操作系统，无法与外网进行联网监控操作运行，使得该系统的实用性及性价比受到了业内高端市场发展需求的挑战。
在次氯酸钠制备过程中，需要使用饱和盐水来配制3％左右的盐水作为电解槽的电解溶液，中国专利申请201420290748.5采用了气体混合溶液产生饱和盐水溶液的方法，由于气泡从下而上造成食盐和溶液翻腾，在流出的溶液中会有大量没有溶解的食盐存在，影响后续稀盐水的配制，且结构较为复杂。
在次氯酸钠制备过程中，盐水自动配比装置大都采用水泵增压给供水管道进行供水，随着水泵的启动或停止会使得管道的水压力产生变化，造成相同通径的出水孔所流过的流量有较大差异。中国专利申请CN201020141294.7公开了一种用于管道水压水流控制的自动恒压恒流阀，它是通过弹簧的间隙的变化来达到水流量不受压力变化而实现恒定控制的目的，但弹簧钢长期浸泡在在水中，不可避免的会导致锈蚀，导致弹簧的弹性系数变化，因此弹簧的间隙也会变化，导致流量不稳定等，很难真正的实现恒定控制水流量。
在次氯酸钠制备过程中，电解装置因受硬质水源条件的限制，而使得次氯酸钠发生器装置的电解槽的电极表面结垢及挂有附着物等，其电解效率明显下降。目前常用电解前常温预制软化水防结垢、设置电极倒极除垢、给电解槽降温防结垢以及利用超声波发泡阻结垢等解决方案，但都还不能满足有效防止电极表面结垢等的难题。中国专利申请201511033467.7公开了“一种电化杀菌水处理器”， 能够实现电解槽在反应一定时间之后发生正负电极切换，电极瞬时增大电流来去除阴极上的污垢结垢的效果，但电极受损较大，导致电极的寿命大大缩短，且需要实时停机处理，影响电解槽的连续运行，降低电解槽的运行效率。
中国专利申请201120289631.1公开了一种“一体化全自动饮用水消毒装置”，主要由整流控制柜、软化器、溶盐箱、浓盐水泵、电解发生器、次氯酸钠贮箱和加药泵构成，以实现全自动连续工作、经济性及实用性强的目的。中国专利申请201520262103.5公开了一种“全自动静态式次氯酸钠发生器”，包括整流器、溶盐箱、软水器、电解箱、储罐、自来水进管、氢气排管、盐水投加泵、次氯酸钠投加泵、软水进水电动阀和次氯酸钠出液电动阀构成，以实现提高自动化程度和电解效率等目的。但这些方案还存在以下明显不足：一是所谓全自动还仅于对单套水处理设备中各单元装置的PLC控制，不具有外网联网功能，无法与外网的总控制平台进行联网运行监控管理；二是因与外网的总控制平台无联网运行功能，用户单套水处理设备运行中可能出现的故障无法实时自动排除，直接影响运行的可靠性；三是不具有外网联网功能的单套水处理设备的运行效率不高，不仅对实时排故受影响，而且对运行、停运和维护等也受影响，即不具有与外网联网的自助功能。
综上所述，如何克服现有技术所存在的不足已成为当今生活用水处理设备技术领域中亟待解决的重点难题之一。
发明内容
本发明的目的是为克服现有技术所存在的不足而提供一种基于改进型的全自动次氯酸钠发生器系统及实现方法，本发明通过采用联网用户工位终端以及改进的溶盐装置、自动配比装置和电解装置，既大大优化了内网运行操作的单元设备，又满足了与外网联网运行监控管理的需要，从而显著地提高全自动次氯酸钠发生器系统的运行效率。
根据本发明提出的一种基于改进型的全自动次氯酸钠发生器系统，包括溶盐装置、自动配比装置、电解装置和投加装置，各功能装置依次串联连接，各功能装置中均设有控制单元并分别通过数据线与PLC控制台信号连接，其特征在于，还包括联网用户工位终端,所述联网用户工位终端通过数据线与PLC控制台信 号连接，还与外网监控系统进行交互式无线数据通信；所述溶盐装置包括阶梯式溶盐设备、自动配比装置包括液体恒流控制器、电解装置包括集成式防结垢的电解设备，其中：
所述联网用户工位终端包括数据处理器分别与信号转换模块、无线数据通信模块、次氯酸钠发生器装置的状态数据采集模块、次氯酸钠发生器装置的自助操作程序数据模块、故障排除操作程序数据模块和视音频提示器信号连接，以及为所述联网用户工位终端供电的电源管理模块；所述信号转换模块包括用于转换所述联网用户工位终端输入和输出信号的模数转换模块和数模转换模块。
所述阶梯式溶盐设备，包括进水口、出液口、桶盖、桶身、桶底、喷水管和阶梯式盐槽结构，所述喷水管与进水口相连通，固定于桶身的上部，喷水管下设有均匀分布的喷水孔；所述阶梯式盐槽结构包括设有首层盐槽和底层盐槽，首层盐槽为环形槽结构，桶身与首层盐槽为一体结构；底层盐槽为圆形结构，桶底与底层盐槽为一体结构；在底层盐槽与桶身之间为饱和盐水槽，饱和盐水槽与出液口相连通；
所述液体恒流控制器，包括上阀体、下阀体、弹性垫和阀芯，所述上阀体设有内螺纹，所述下阀体设有和上阀体相配合的外螺纹，上阀体和下阀体通过内外螺纹连接并形成上阀体和下阀体组合后的阀体空腔，所述阀体空腔内，沿上阀体至下阀体的轴向依次设有带孔的弹性垫和可活动的阀芯，所述可活动的阀芯包括半圆形密封部和圆筒状导向部，半圆形密封部的外表面设有凸起，所述圆筒形导向部的圆周壁上设有可供液体流通的阀芯通孔，所述带孔的弹性垫设有与所述半圆形密封部贴合的密封面；
所述集成式防结垢的电解设备，包括洁净盐水釜通过带液体输流管的液体增流泵与区隔式电解群连接；所述洁净盐水釜包括带加热器的盐水加热釜与带滤清材料的热盐水滤清釜毗联，所述洁净盐水加热釜中的盐水温度为50-100℃；所述液体增流泵的功率为10-100w、扬程为25-35m；所述区隔式电解群包括2至N个电解釜，其中每个电解釜之间通过液体增流管连接；每个电解釜内均设有包括阳极极板与阴极极板的单对电极，所述单对电极与电解釜外部的直流电源连接；所述区隔式电解群中的电解液的液流速度不小于洁净盐水釜中的盐水的水流速度。
本发明的实现原理是：本发明提出的一种基于改进型的全自动次氯酸钠发生器系统及实现方法是对现有传统的全自动次氯酸钠发生器系统的综合性技术改进，具体是：配制饱和盐水的溶盐装置为阶梯式溶盐设备，可利用水自身的动能和势能从高处多次冲击混合盐仓中的盐，将盐与水充分混合；自动配比装置中采用了液体恒流控制器，可使液体流道的截面随着液体压力的变化呈现反比例变化，从而确保了液体流量恒定不变；电解装置为集成式防结垢的电解设备，采用电解前预制洁净高温盐水、增加液流速度和多釜区隔式电解的新方案，它集除垢、防垢和阻垢的措施于一体，且很好地发挥了协同防结垢的作用；联网用户工位终端与PLC控制台协同构建既可实现与本系统各功能单元进行内网运行操作，又可与外网联网运行监控管理，不仅大大优化了内网运行操作的单元设备，又满足了与外网联网运行监控管理的需要。
本发明与现有技术相比其显著优点在于：
第一，本发明是针对现有公知的溶盐装置、自动配比装置、电解装置和PLC控制装置等单元装置还存在设计不够合理、配置不够优化和运行效率不高等难题而提出的一种改进型的全自动次氯酸钠发生器系统，且各单元装置发挥了很好的协同作用，因此本发明的实用性及性价比显著提高，能够满足本领域高端市场发展的需求。
第二，本发明构建的集成式防结垢的次氯酸钠发生器装置，通过在电解前采取预制洁净盐水、增加液流速度以及多釜区隔式电解等措施，发挥了很好的集成式的除垢、防垢和阻垢的协同作用，取得了比现有技术防结垢措施更加显著的效果。
第三，本发明构建的配制饱和盐水的溶盐装置为阶梯式盐槽装置，可利用水自身的动能和势能从高处多次冲击混合盐仓中的盐，确保盐与水充分混合，提高饱和盐水配制的效率。
第四，本发明构建的用于自动配比装置的液体流量恒定控制装置，可使液体流道的截面随着液体压力的变化呈现反比例变化，从而确保了液体流量恒定不变，满足了精准计量的需要。
第五，本发明构建的联网用户工位终端既可通过PLC控制台与本系统各功能单元装置进行内网运行操作，又可与外网联网运行监控管理，大大地提高了改进 型的全自动次氯酸钠发生器系统的运行可靠性和效能。
附图说明
图1为本发明提出的一种基于改进型的全自动次氯酸钠发生器系统的内网结构方框示意图。
图2为本发明提出的一种基于改进型的全自动次氯酸钠发生器系统的内网与外网联网的结构方框示意图。
图3为本发明提出的阶梯式溶盐设备的剖面结构示意图。
图4为本发明提出的联网用户工位终端的结构方框示意图。
图5为本发明提出的液体恒流控制器的结构示意图；图5包括图5-1、图5-2、图5-3、图5-4、图5-5、图5-6、图5-7；其中：图5-1为立体结构示意图；图5-2为整体剖面结构示意图；图5-3为阀体空腔剖面结构示意图；图5-4为弹性垫的立体结构示意图；图5-5为弹性垫的剖面结构示意图；图5-6为可活动的阀芯的立体结构示意图；图5-7为可活动的阀芯的剖面结构示意图。
图6为本发明提出的集成式防结垢的电解装置的立式结构示意图。
图7为本发明提出的集成式防结垢的电解装置的卧式结构示意图。
图8为本发明提出的一种基于改进型的全自动次氯酸钠发生器系统的实现方法的流程方框示意图。
具体实施方式
下面结合附图和实施例对本发明的具体实施方式作进一步的详细说明。
实施例1。结合图1，本发明提出的一种基于改进型的全自动次氯酸钠发生器系统，包括溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)，各功能装置通过连接管(5)依次串联连接，各功能装置中均设有控制单元并分别通过数据线(6)与PLC控制台(7)信号连接，其特征在于，还包括联网用户工位终端(8),所述联网用户工位终端(8)通过数据线(6)与PLC控制台(7)信号连接，还与外网监控系统(9)进行交互式无线数据通信；所述溶盐装置(1)包括阶梯式溶盐设备、自动配比装置(2)包括液体恒流控制器、电解装置(3)包括集成式防结垢的电解设备。结合图2，本发明提出的一种基 于改进型的全自动次氯酸钠发生器系统的优选方案在于所述外网监控系统(9)包括后台云端服务器、无线数据通信网络和智能远程群控自助服务器，所述无线数据通信网络分别与后台云端服务器和智能远程群控自助服务器进行数据通信连接；所述后台云端服务器通过无线数据通信网络支持智能群控自助服务器与联网用户工位终端进行交互式数据通信。因此，本发明既可通过联网用户工位终端(8)与本系统各功能单元进行内网运行操作，而且本发明还可通过联网用户工位终端(8)与外网联网运行监控管理，确实提高改进型的全自动次氯酸钠发生器系统的运行可靠性和效能。
实施例2。结合图3，本发明所述联网用户工位终端(8)包括数据处理器分别与信号转换模块、无线数据通信模块、次氯酸钠发生器装置的状态数据采集模块、次氯酸钠发生器装置的自助操作程序数据模块、故障排除操作程序数据模块和视音频提示器信号连接，以及为所述联网用户工位终端供电的电源管理模块；所述信号转换模块包括用于转换所述联网用户工位终端输入和输出信号的模数转换模块和数模转换模块。
实施例3。结合图4，本发明所述阶梯式溶盐设备，包括进水口(1-1)、出液口(1-2)、桶盖(1-3)、桶身(1-4)、桶底(1-5)、喷水管(1-6)和阶梯式盐槽结构，所述喷水管(1-6)与进水口(1-1)相连通，固定于桶身(1-4)的上部，喷水管(1-6)下设有均匀分布的喷水孔；所述阶梯式盐槽结构包括设有首层盐槽(1-7.1)和底层盐槽(1-7.2)，首层盐槽(1-7.1)为环形槽结构，桶身(1-4)与首层盐槽(1-7.1)为一体结构；底层盐槽(1-7.2)为圆形结构，桶底(1-5)与底层盐槽(1-7.2)为一体结构；在底层盐槽(1-7.2)与桶身(1-4)之间为饱和盐水槽，饱和盐水槽与出液口(1-2)相连通。其优选方案还包括在所述首层盐槽(1-7.1)与底层盐槽(1-7.2)之间设置环形结构的中间层盐槽(1-7.3)，所述中间层盐槽(1-7.3)的槽口宽度从首层盐槽(1-7.1)开始到各中间层盐槽(1-7.3)逐步加宽，形成阶梯形结构，中间层盐槽(1-7.3)设置为一层或多层，桶身(4)与中间层盐槽(1-7.3)为一体结构。
实施例4。结合图5，本发明所述液体恒流控制器，包括上阀体(2-1)、下阀体(2-2)、弹性垫(2-3)和可活动的阀芯(2-4)，所述上阀体(2-1)设有内螺纹(2-1.1)，所述下阀体(2-2)设有和上阀体(2-1)相配合的外螺纹 (2-2.1)，上阀体(2-1)和下阀体(2-2)通过内外螺纹连接并形成上阀体(2-1)和下阀体(2-2)组合后的阀体空腔(2-5)，所述阀体空腔(2-5)内，沿上阀体(2-1)至下阀体(2-2)的轴向依次设有带孔的弹性垫(2-3)和可活动的阀芯(2-4)，所述可活动的阀芯(2-4)包括半圆形的密封部(2-4.1)和圆筒状的导向部(2-4.2)，半圆形的密封部(2-4.1)的外表面设有凸起(2-4.4)，所述圆筒形的导向部(2-4.2)的圆周壁上设有可供液体流通的阀芯通孔(2-4.3)，所述带孔的弹性垫(2-3)设有与所述半圆形的密封部(2-4.1)贴合的密封面(2-3.1)；所述带孔的弹性垫(2-3)为圆柱状，其轴向设有可供液体流过的弹性垫通孔(2-3.2)，弹性垫通孔(2-3.2)的直径为0.1-5mm。其优选方案还包括所述圆筒形的导向部(2-4.2)与下阀体(2-2)之间设有供液体流通的间隙(2-6)，所述间隙(2-6)的宽度为0.2-5mm；所述凸起(2-4.4)的形状为半球形，所述凸起(2-4.4)的高度为0.2-5mm；所述上阀体(2-1)和下阀体(2-2)的材质均为不锈钢、铜合金、铝合金或工程塑料；所述带孔的弹性垫(2-3)的材质为橡胶、硅胶或硅橡胶；所述可活动阀芯(2-4)的材质为陶瓷或工程塑料。
实施例5。结合图6和图7，本发明所述集成式防结垢的电解设备，包括洁净盐水釜通过带液体输流管(3-6)的液体增流泵(3-5)与区隔式电解群(3-9)连接；所述洁净盐水釜包括带加热器(3-3)的盐水加热釜(3-1)与带滤清材料(3-4)的热盐水滤清釜(3-2)毗联，所述洁净盐水加热釜(3-1)中的盐水温度为50-100℃；所述液体增流泵(3-5)的功率为10-100w、扬程为25-35m；所述区隔式电解群(3-9)包括2至N个电解釜，其中每个电解釜之间通过液体增流管(3-8)连接；每个电解釜内均设有包括阳极极板与阴极极板的单对电极(3-7)，所述单对电极(3-7)与电解釜外部的直流电源连接；所述区隔式电解群(3-9)中的电解液的液流速度不小于洁净盐水釜中的盐水的水流速度。其优选方案还包括：所述盐水加热釜(3-1)的加热器(3-3)设置在盐水加热釜(3-1)的内部或盐水加热釜(3-1)的外部；所述盐水加热釜(3-1)中的盐水温度为70℃；所述热盐水滤清釜(3-2)的滤清材料(3-4)为天然沸石或离子交换树脂；所述集成式防结垢的电解设备中的液体增流泵(3-5)的电功率为40w、扬程为30米；洁净盐水釜中的热盐水的水流速度与区隔式电解群(3-9)中的电解液的液流速度均不小于1米/秒；所述液体增流管(3-8)的管口直径为液体输流管(3-6) 的管口直径的1/2至3/4。
实施例6。结合图8，本发明提出的一种基于改进型的全自动次氯酸钠发生器系统的实现方法，包括如下具体步骤：
步骤1，开机联网控制：用户端的全自动次氯酸钠发生器设备的运行工作准备就绪，用户打开联网用户工位终端(8)的用户设备登录账户，输入对应用户端的启动信息，指令PLC控制台与溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)的各控制单元构建的内网操作控制系统进入启动状态；同时联网用户工位终端(8)把对应用户端的开机信息上报给外网监控系统(9)并完成对反馈指令的接收，直至用户端的全自动次氯酸钠发生器设备开机联网成功并进入运行状态；
步骤2，联网运行控制：步骤1所述用户端的全自动次氯酸钠发生器设备开机联网成功并进入运行状态后，溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)的各控制单元分别接受PLC控制台(7)发给的指令并实施各功能单元的控制，同时联网用户工位终端(8)把PLC控制台(7)集成的内网操作控制系统的运行控制信息上报给外网监控系统(9)备份；
步骤3，联网排故控制：步骤2所述联网运行控制中，若出现对应用户端的全自动次氯酸钠发生器设备运行失常的状况，则外网监控系统会根据对应用户端的联网用户工位终端(8)上报的运行控制信息给出指令联网用户工位终端(8)进行故障排除操作的信息提示,直至对应用户端的全自动次氯酸钠发生器设备由运行失常转为运行正常，同时联网用户工位终端(8)把排故信息上报给外网监控系统(9)备份；
步骤4，关机联网控制：当对应用户端的全自动次氯酸钠发生器设备需要停止运行并关机时,联网用户工位终端(8)把对应用户端的全自动次氯酸钠发生器设备的关机停运信息上报外网监控系统(9)，所述外网监控系统(9)则根据上报的关机停运信息给出对应用户端的联网用户工位终端(8)关机及后续对全自动次氯酸钠发生器设备进行清理操作程序的信息提示,直至对应用户端的全自动次氯酸钠发生器设备完成清理操作程序并上报清理操作信息给外网监控系统(9)，以备份对应用户端的全自动次氯酸钠发生器设备已进入停止运行的状态。
本发明的具体实施方式中凡未涉到的说明属于本领域的公知技术，可参考公 知技术加以实施。
本发明经反复试验验证，取得了满意的试用效果。
以上具体实施方式及实施例是对本发明提出的一种基于改进型的全自动次氯酸钠发生器系统及实现方法技术思想的具体支持，不能以此限定本发明的保护范围，凡是按照本发明提出的技术思想，在本技术方案基础上所做的任何等同变化或等效的改动，均仍属于本发明技术方案保护的范围。

Claims (10)

  1. 一种基于改进型的全自动次氯酸钠发生器系统，包括溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)，各功能装置通过连接管(5)依次串联连接，各功能装置中均设有控制单元并分别通过数据线(6)与PLC控制台(7)信号连接，其特征在于，还包括联网用户工位终端(8),所述联网用户工位终端(8)通过数据线(6)与PLC控制台(7)信号连接，还与外网监控系统(9)进行交互式无线数据通信；所述溶盐装置(1)包括阶梯式溶盐设备、自动配比装置(2)包括液体恒流控制器、电解装置(3)包括集成式防结垢的电解设备，其中：
    所述联网用户工位终端(8)包括数据处理器分别与信号转换模块、无线数据通信模块、次氯酸钠发生器装置的状态数据采集模块、次氯酸钠发生器装置的自助操作程序数据模块、故障排除操作程序数据模块和视音频提示器信号连接，以及为所述联网用户工位终端(8)供电的电源管理模块；所述信号转换模块包括用于转换所述联网用户工位终端(8)输入和输出信号的模数转换模块和数模转换模块。
    所述阶梯式溶盐设备，包括进水口(1-1)、出液口(1-2)、桶盖(1-3)、桶身(1-4)、桶底(1-5)、喷水管(1-6)和阶梯式盐槽结构，所述喷水管(1-6)与进水口(1-1)相连通，固定于桶身(1-4)的上部，喷水管(1-6)下设有均匀分布的喷水孔；所述阶梯式盐槽结构包括设有首层盐槽(1-7.1)和底层盐槽(1-7.2)，首层盐槽(1-7.1)为环形槽结构，桶身(1-4)与首层盐槽(1-7.1)为一体结构；底层盐槽(1-7.2)为圆形结构，桶底(1-5)与底层盐槽(1-7.2)为一体结构；在底层盐槽(1-7.2)与桶身(1-4)之间为饱和盐水槽，饱和盐水槽与出液口(1-2)相连通；
    所述液体恒流控制器，包括上阀体(2-1)、下阀体(2-2)、弹性垫(2-3)和可活动的阀芯(2-4)，所述上阀体(2-1)设有内螺纹(2-1.1)，所述下阀体(2-2)设有和上阀体(2-1)相配合的外螺纹(2-2.1)，上阀体(2-1)和下阀体(2-2)通过内外螺纹连接并形成上阀体(2-1)和下阀体(2-2)组合后的阀体空腔(2-5)，所述阀体空腔(2-5)内，沿上阀体(2-1)至下阀体(2-2)的轴向依次设有带孔的弹性垫(2-3)和可活动的阀芯(2-4)，所述可活动的阀芯(2-4)包括半圆形的密封部(2-4.1)和圆筒状的导向部(2-4.2)，半圆形的密封部(2-4.1)的外表面设有凸起(2-4.4)，所述圆筒形的导向部(2-4.2)的圆周壁上设有可供液体流通的阀芯通孔(2-4.3)，所述带孔的弹性垫(2-3)设有与所述半圆形的密封部(2-4.1)贴合的密封面(2-3.1)；所述带孔的弹性垫(2-3)为圆柱状，其轴向设有可供液体流过的弹性垫通孔(2-3.2)，弹性垫通孔(2-3.2)的直径为0.1-5mm；
    所述集成式防结垢的电解设备，包括洁净盐水釜通过带液体输流管(3-6)的液体增流泵(3-5)与区隔式电解群(3-9)连接；所述洁净盐水釜包括带加热器(3-3)的盐水加热釜(3-1) 与带滤清材料(3-4)的热盐水滤清釜(3-2)毗联，所述洁净盐水加热釜(3-1)中的盐水温度为50-100℃；所述液体增流泵(3-5)的功率为10-100w、扬程为25-35m；所述区隔式电解群(3-9)包括2至N个电解釜，其中每个电解釜之间通过液体增流管(3-8)连接；每个电解釜内均设有包括阳极极板与阴极极板的单对电极(3-7)，所述单对电极(3-7)与电解釜外部的直流电源连接；所述区隔式电解群(3-9)中的电解液的液流速度不小于洁净盐水釜中的盐水的水流速度。
  2. 根据权利要求1所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述外网监控系统(9)包括后台云端服务器、无线数据通信网络和智能远程群控自助服务器，所述无线数据通信网络分别与后台云端服务器和智能远程群控自助服务器进行数据通信连接；所述后台云端服务器通过无线数据通信网络支持智能群控自助服务器与联网用户工位终端进行交互式数据通信。
  3. 根据权利要求2所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述阶梯式溶盐设备还包括在首层盐槽(1-7.1)与底层盐槽(1-7.2)之间设置环形结构的中间层盐槽(1-7.3)，所述中间层盐槽(1-7.3)的槽口宽度从首层盐槽(1-7.1)开始到各中间层盐槽(1-7.3)逐步加宽，形成阶梯形结构，中间层盐槽(1-7.3)设置为一层或多层，桶身(4)与中间层盐槽(1-7.3)为一体结构。
  4. 根据权利要求3所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述圆筒形的导向部(2-4.2)与下阀体(2-2)之间设有供液体流通的间隙(2-6)，所述间隙(2-6)的宽度为0.2-5mm；所述凸起(2-4.4)的形状为半球形，所述凸起(2-4.4)的高度为0.2-5mm。
  5. 根据权利要求4所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述盐水加热釜(3-1)的加热器(3-3)设置在盐水加热釜(3-1)的内部或盐水加热釜(3-1)的外部；所述盐水加热釜(3-1)中的盐水温度为70℃。
  6. 根据权利要求5所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述热盐水滤清釜(3-2)的滤清材料(3-4)为天然沸石或离子交换树脂。
  7. 根据权利要求6所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述集成式防结垢的电解设备中的液体增流泵(3-5)的电功率为40w、扬程为30米。
  8. 根据权利要求7所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于，所述集成式防结垢的电解设备中的洁净盐水釜中的热盐水的水流速度与区隔式电解群(3-9)中的电解液的液流速度均不小于1米/秒。
  9. 根据权利要求8所述的一种基于改进型的全自动次氯酸钠发生器系统，其特征在于， 所述集成式防结垢的电解设备中的液体增流管(3-8)的管口直径为液体输流管(3-6)的管口直径的1/2至3/4。
  10. 根据权利要求1-9任一项所述的一种基于改进型的全自动次氯酸钠发生器系统的实现方法，其特征在于，包括如下具体步骤：
    步骤1，开机联网控制：用户端的全自动次氯酸钠发生器设备的运行工作准备就绪，用户打开联网用户工位终端(8)的用户设备登录账户，输入对应用户端的启动信息，指令PLC控制台与溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)的各控制单元构建的内网操作控制系统进入启动状态；同时联网用户工位终端(8)把对应用户端的开机信息上报给外网监控系统(9)并完成对反馈指令的接收，直至用户端的全自动次氯酸钠发生器设备开机联网成功并进入运行状态；
    步骤2，联网运行控制：步骤1所述用户端的全自动次氯酸钠发生器设备开机联网成功并进入运行状态后，溶盐装置(1)、自动配比装置(2)、电解装置(3)和投加装置(4)的各控制单元分别接受PLC控制台(7)发给的指令并实施各功能单元的控制，同时联网用户工位终端(8)把PLC控制台(7)集成的内网操作控制系统的运行控制信息上报给外网监控系统(9)备份；
    步骤3，联网排故控制：步骤2所述联网运行控制中，若出现对应用户端的全自动次氯酸钠发生器设备运行失常的状况，则外网监控系统会根据对应用户端的联网用户工位终端(8)上报的运行控制信息给出指令联网用户工位终端(8)进行故障排除操作的信息提示,直至对应用户端的全自动次氯酸钠发生器设备由运行失常转为运行正常，同时联网用户工位终端(8)把排故信息上报给外网监控系统(9)备份；
    步骤4，关机联网控制：当对应用户端的全自动次氯酸钠发生器设备需要停止运行并关机时,联网用户工位终端(8)把对应用户端的全自动次氯酸钠发生器设备的关机停运信息上报外网监控系统(9)，所述外网监控系统(9)则根据上报的关机停运信息给出对应用户端的联网用户工位终端(8)关机及后续对全自动次氯酸钠发生器设备进行清理操作程序的信息提示,直至对应用户端的全自动次氯酸钠发生器设备完成清理操作程序并上报清理操作信息给外网监控系统(9)，以备份对应用户端的全自动次氯酸钠发生器设备已进入停止运行的状态。
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