CN204281425U - A kind of marine circulating cooling system system water process regulator control system - Google Patents
A kind of marine circulating cooling system system water process regulator control system Download PDFInfo
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- CN204281425U CN204281425U CN201420748306.0U CN201420748306U CN204281425U CN 204281425 U CN204281425 U CN 204281425U CN 201420748306 U CN201420748306 U CN 201420748306U CN 204281425 U CN204281425 U CN 204281425U
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Abstract
本实用新型涉及海水循环冷却水处理技术领域,具体涉及一种海水循环冷却系统水处理调控系统,包括海水循环冷却系统、控制柜(21)和微机管理控制系统(22),所述海水循环冷却系统的管线依次连接集水池(5)、海水循环泵(6)、热交换器(10)和海水冷却塔(11),在集水池(5)入口设置有海水补水系统和加药系统,在海水循环泵(6)出口设置有循环水排污系统,各系统通过与控制柜中的流量、液位、电导率监测仪表和PLC连接,PLC连接微机系统实现统一管理控制。本实用新型可实现海水循环冷却系统补水、排污、加药的自动化管理控制,能有力保障海水循环冷却系统的水平衡、浓缩倍数控制和水处理效果,保证海水循环冷却系统的安全稳定运行。
The utility model relates to the technical field of seawater circulating cooling water treatment, in particular to a water treatment control system for a seawater circulating cooling system, comprising a seawater circulating cooling system, a control cabinet (21) and a microcomputer management control system (22). The pipelines of the system are sequentially connected to the sump (5), the seawater circulation pump (6), the heat exchanger (10) and the seawater cooling tower (11). The outlet of the seawater circulation pump (6) is provided with a circulating water sewage system, and each system is connected to the flow, liquid level, conductivity monitoring instrument in the control cabinet and PLC, and the PLC is connected to the microcomputer system to realize unified management and control. The utility model can realize the automatic management and control of water replenishment, sewage discharge and chemical dosing of the seawater circulation cooling system, can effectively guarantee the water balance, concentration multiple control and water treatment effect of the seawater circulation cooling system, and ensure the safe and stable operation of the seawater circulation cooling system.
Description
技术领域technical field
本实用新型涉及海水循环冷却水处理技术领域,主要涉及一种海水循环冷却系统水处理调控系统。The utility model relates to the technical field of seawater circulation cooling water treatment, and mainly relates to a water treatment control system of a seawater circulation cooling system.
背景技术Background technique
海水循环冷却技术是一项环保型新技术,国外经过30多年的发展,现已进入大规模应用阶段。随着我国沿海水资源短缺问题的加剧和海水循环冷却技术的日趋成熟,沿海企业逐渐加大海水利用力度,纷纷投建海水循环冷却工程。其中,我国沿海电厂新建装机容量1000MW以上的机组已建成、在建、待建的不下10台,单台海水循环冷却水量均在每小时十万吨以上。Seawater circulating cooling technology is an environmentally friendly new technology. After more than 30 years of development abroad, it has entered the stage of large-scale application. With the aggravation of the shortage of coastal water resources in my country and the maturity of seawater circulation cooling technology, coastal enterprises have gradually increased the use of seawater and invested in the construction of seawater circulation cooling projects. Among them, my country's coastal power plants have built more than 10 units with an installed capacity of more than 1000 MW, and there are no less than 10 units under construction or to be built.
面对当前沿海企业对海水循环冷却技术的迫切需求,我国海水循环冷却技术经过十余年的连续科技攻关,取得了重大技术突破,已完成百吨级、千吨级、万吨级、十万吨级示范工程。并形成系列化海水水处理药剂产品,基本具备大规模化推广应用的技术条件。而相比之下,海水循环冷却系统水处理管理技术研究还显得薄弱和滞后,无论是现场技术监测和参数调节控制都还是人工手动,没有实现自动化控制和计算机管理。在精度控制上还存在很大的不确定性和随机性,这对于海水循环冷却技术的系统安全和稳定运行存在很大的隐患。Facing the urgent needs of coastal enterprises for seawater circulating cooling technology, my country's seawater circulating cooling technology has achieved major technological breakthroughs after more than ten years of continuous scientific and technological research, and has completed hundred-ton, thousand-ton, 10,000-ton, 100,000-ton Ton level demonstration project. And form a series of seawater treatment pharmaceutical products, basically have the technical conditions for large-scale promotion and application. In contrast, the research on water treatment management technology of seawater circulating cooling system is still weak and lagging behind. Both on-site technical monitoring and parameter adjustment control are still manual, and automatic control and computer management have not been realized. There is still a lot of uncertainty and randomness in the precision control, which poses a great hidden danger to the safe and stable operation of the seawater circulating cooling technology.
为解决冷却水现场管理中存在的相关问题,国内外在这一方面的研究和应用都十分活跃。主要包括工艺参数的在线监测,实现自动加药、自动排污、水平衡控制等。从技术角度讲,国内外在淡水循环冷却系统水处理管理控制方面的技术应用已基本成熟,而在海水冷却系统中的应用报道较少。包括当前国际上最先进的Nalco公司开发的3D-TRASAR管理系统,在海水冷却体系中也未应用先例。In order to solve the relevant problems in the on-site management of cooling water, the research and application in this area are very active at home and abroad. It mainly includes on-line monitoring of process parameters, automatic dosing, automatic sewage discharge, water balance control, etc. From a technical point of view, the technical application of water treatment management and control in fresh water circulating cooling systems at home and abroad has been basically mature, while there are few reports on the application in seawater cooling systems. Including the most advanced 3D-TRASAR management system developed by Nalco in the world, there is no precedent for seawater cooling system.
实用新型内容Utility model content
本实用新型解决的技术问题是:由于海水含盐量高,具有腐蚀性和成垢性离子远高于淡水,海水循环水浓缩倍数的控制和水处理药剂的使用与现有技术有很大差别,一些检监测技术在海水体系中会受到很大的干扰或限制。因此,如何在现有基础上,借鉴国内外先进经验,整合集成现有技术,结合海水的特点,优化管理控制系统设计,实现海水循环水处理运行管理,保障海水循环冷却系统的安全稳定运行已十分迫切。The technical problem solved by the utility model is: due to the high salt content of seawater, corrosive and scaling ions are much higher than that of fresh water, the control of the concentration multiple of seawater circulating water and the use of water treatment chemicals are very different from the prior art , some detection and monitoring technologies will be greatly disturbed or restricted in seawater systems. Therefore, on the existing basis, how to learn from the advanced experience at home and abroad, integrate the existing technology, combine the characteristics of seawater, optimize the design of the management and control system, realize the operation management of seawater circulating water treatment, and ensure the safe and stable operation of the seawater circulating cooling system. very urgent.
针对现有技术,本实用新型提供一种海水循环冷却系统水处理调控系统,实现海水循环冷却系统补水、排污、加药的自动化管理控制,有力保障海水循环冷却系统的水平衡、浓缩倍数控制和水处理效果,保证海水循环冷却系统的安全稳定运行。Aiming at the prior art, the utility model provides a water treatment control system of the seawater circulation cooling system, which realizes the automatic management and control of water replenishment, sewage discharge and drug dosing of the seawater circulation cooling system, and effectively guarantees the water balance, concentration ratio control and The water treatment effect ensures the safe and stable operation of the seawater circulating cooling system.
具体来说,针对现有技术的不足,本实用新型提供了如下技术方案:Specifically, for the deficiencies in the prior art, the utility model provides the following technical solutions:
一种海水循环冷却系统水处理调控系统,包括海水循环冷却系统、控制柜21和微机调控系统22,其特征在于,所述海水循环冷却系统的管线依次连接集水池5、海水循环泵6、热交换器10和海水冷却塔11,在集水池5入口设置有海水补水系统和加药系统,在海水循环泵6出口设置有循环水排污系统,所述海水补水系统、加药系统和循环水排污系统都安装有与控制柜21的监测仪表连接的流量、液位或电导率测量装置,并都安装有与控制柜21的可编程逻辑控制器连接的输送泵或电动阀。A water treatment control system of a seawater circulation cooling system, comprising a seawater circulation cooling system, a control cabinet 21 and a microcomputer control system 22, characterized in that the pipelines of the seawater circulation cooling system are sequentially connected to a sump 5, a seawater circulation pump 6, a heat sink The exchanger 10 and the seawater cooling tower 11 are provided with a seawater replenishment system and a dosing system at the inlet of the sump 5, and a circulating water sewage system is provided at the outlet of the seawater circulation pump 6, and the seawater replenishment system, the dosing system and the circulating water sewage The systems are all equipped with flow, liquid level or conductivity measuring devices connected to the monitoring instruments of the control cabinet 21, and are all equipped with delivery pumps or electric valves connected with the programmable logic controller of the control cabinet 21.
优选的,上述海水循环冷却系统水处理调控系统中,所述控制柜21的各个监测仪表与可编程逻辑控制器连接,所述可编程逻辑控制器通过总线与微机管理控制系统22连接。Preferably, in the above-mentioned water treatment control system of the seawater circulation cooling system, each monitoring instrument of the control cabinet 21 is connected to a programmable logic controller, and the programmable logic controller is connected to the microcomputer management control system 22 through a bus.
优选的,上述海水循环冷却系统水处理调控系统中,所述海水补水系统包括与海水相连的变频海水泵1、补水电动阀2、海水补水流量计3和安装在集水池5中的第一液位传感器4,所述变频海水泵1和补水电动阀2与控制柜21的可编程逻辑控制器连接,所述海水补水流量计3和第一液位传感器4与控制柜21的流量和液位监测仪表连接。Preferably, in the above-mentioned water treatment control system of the seawater circulation cooling system, the seawater replenishment system includes a frequency conversion seawater pump 1 connected to the seawater, a replenishment electric valve 2, a seawater replenishment flow meter 3 and a first liquid pump installed in the sump 5 The level sensor 4, the frequency conversion seawater pump 1 and the replenishment electric valve 2 are connected to the programmable logic controller of the control cabinet 21, the seawater replenishment flow meter 3 and the first liquid level sensor 4 are connected to the flow and liquid level of the control cabinet 21 Monitor instrumentation connections.
优选的,上述海水循环冷却系统水处理调控系统中,在海水循环泵6出口设置有排污支管线和连接海水循环泵出口和集水池入口的回水支路,所述循环水排污系统包括在回水支路安装的海水电导率传感器7、排污支管线安装的排污电动阀8和排污流量计9,所述排污电动阀8与控制柜21的可编程逻辑控制器连接,所述海水电导率传感器7和排污流量计9与控制柜21的电导率和流量监测仪表连接。Preferably, in the water treatment control system of the above-mentioned seawater circulation cooling system, a sewage branch line and a return water branch connecting the seawater circulation pump outlet and the sump inlet are provided at the outlet of the seawater circulation pump 6, and the circulating water sewage system includes The seawater conductivity sensor 7 installed in the water branch, the blowdown electric valve 8 and the blowdown flow meter 9 installed in the blowdown branch line, the blowdown electric valve 8 is connected to the programmable logic controller of the control cabinet 21, and the seawater conductivity sensor 7 and sewage flow meter 9 are connected with the conductivity and flow monitoring instrument of control cabinet 21.
优选的,上述海水循环冷却系统水处理调控系统中,所述加药系统包括海水阻垢缓蚀剂加药系统和海水菌藻抑制剂加药系统。Preferably, in the water treatment control system of the seawater circulating cooling system, the dosing system includes a dosing system for seawater scale and corrosion inhibitors and a dosing system for seawater bacteria and algae inhibitors.
优选的,上述海水循环冷却系统水处理调控系统中,所述海水阻垢缓蚀剂加药系统包括安装有第二液位传感器12的第一储备罐13、药剂输送泵14和安装有计量泵16和第三液位传感器17的加药罐15,所述药剂输送泵14和计量泵16与控制柜21的可编程逻辑控制器连接,所述第二液位传感器12和第三液位传感器17与控制柜21的液位监测仪表连接。Preferably, in the above-mentioned seawater circulation cooling system water treatment control system, the seawater scale and corrosion inhibitor dosing system includes a first storage tank 13 with a second liquid level sensor 12 installed, a medicament delivery pump 14 and a metering pump installed 16 and the dosing tank 15 of the third liquid level sensor 17, the medicament delivery pump 14 and the metering pump 16 are connected with the programmable logic controller of the control cabinet 21, the second liquid level sensor 12 and the third liquid level sensor 17 is connected with the liquid level monitoring instrument of control cabinet 21.
优选的,上述海水循环冷却系统水处理调控系统中,所述药剂输送泵14的入口与第一储备罐13连接,出口包括第一支管线和第二支管线,所述第一支管线与加药罐15连接,第二支管线与计量泵16出口管线汇合并共同连接回水支路。Preferably, in the above-mentioned water treatment control system of the seawater circulation cooling system, the inlet of the chemical delivery pump 14 is connected to the first storage tank 13, and the outlet includes a first branch pipeline and a second branch pipeline, and the first branch pipeline is connected to the charging tank 13. The medicine tank 15 is connected, and the second branch pipeline merges with the outlet pipeline of the metering pump 16 and is jointly connected with the return water branch.
优选的,上述海水循环冷却系统水处理调控系统中,所述药剂输送泵14出口第二支管线上与计量泵16出口管线汇合前设置有在基础投加开始浓缩运行阶段开启、在正常运行阶段关闭的第一阀门14a,在计量泵16出口管线上与第二支管线汇合之前设置有在基础投加开始浓缩运行阶段关闭、在正常运行阶段开启的第二阀门16a。Preferably, in the above-mentioned water treatment control system of the seawater circulating cooling system, before the second branch pipeline at the outlet of the agent delivery pump 14 merges with the outlet pipeline of the metering pump 16, it is set to open in the concentration operation stage of the basic dosing, and in the normal operation stage. The closed first valve 14a is provided with a second valve 16a that is closed at the beginning of the basic dosing concentration operation stage and opened at the normal operation stage before the outlet line of the metering pump 16 merges with the second branch line.
优选的,上述海水循环冷却系统水处理调控系统中,所述海水菌藻抑制剂加药系统包括安装有第四液位传感器18的第二储备罐19和加药泵20,所述加药泵20与控制柜21的可编程逻辑控制器连接,所述第四液位传感器18与控制柜21的液位监测仪表连接。Preferably, in the above-mentioned water treatment control system of the seawater circulating cooling system, the seawater bacteria and algae inhibitor dosing system includes a second storage tank 19 equipped with a fourth liquid level sensor 18 and a dosing pump 20, and the dosing pump 20 is connected to the programmable logic controller of the control cabinet 21, and the fourth liquid level sensor 18 is connected to the liquid level monitoring instrument of the control cabinet 21.
优选的,上述海水循环冷却系统水处理调控系统中,所有流量测量装置、液位测量装置、电导率测量装置、输送泵和电动阀中与海水、浓缩海水或药剂直接接触的部件均选用耐海水腐蚀和耐酸碱材料,所述管线选用耐蚀非金属工程材料。Preferably, in the above-mentioned water treatment control system of the seawater circulation cooling system, all flow measuring devices, liquid level measuring devices, conductivity measuring devices, delivery pumps and electric valves that are in direct contact with seawater, concentrated seawater or pharmaceuticals are all made of seawater-resistant Corrosion and acid-alkali-resistant materials, the pipeline is made of corrosion-resistant non-metallic engineering materials.
本实用新型的有益效果是:本实用新型是根据海水本身的特性设计海水循环冷却系统的补水、排污和加药过程,实现海水循环冷却系统水平衡、浓缩倍数和加药排污自动化管理控制,大大提高了系统运行管理水平和控制精度,保障了海水循环冷却水处理效果,使海水循环冷却技术在节水、技术、经济、海洋环境方面更具优势,使我国海水循环冷却技术水平再上新台阶,为大规模产业化推广应用提供强有力的技术支持。The beneficial effects of the utility model are: the utility model is designed according to the characteristics of the seawater itself to replenish water, discharge and dosing process of the seawater circulation cooling system, and realize the automatic management and control of the water balance, the concentration multiple and the dosing and sewage discharge of the seawater circulation cooling system, greatly Improve the system operation management level and control accuracy, guarantee the seawater circulating cooling water treatment effect, make the seawater circulating cooling technology more advantageous in terms of water saving, technology, economy, and marine environment, and bring my country's seawater circulating cooling technology to a new level , to provide strong technical support for large-scale industrial promotion and application.
附图说明Description of drawings
图1是海水循环冷却系统水处理调控系统示意图。Figure 1 is a schematic diagram of the water treatment control system of the seawater circulation cooling system.
图中:1.变频海水泵,2.补水电动阀,3.海水补水流量计,4.第一液位传感器,5.集水池,6.海水循环泵,7.海水电导率传感器,8.排污电动阀,9.排污流量计,10.热交换器,11.海水冷却塔,12.第二液位传感器,13.第一储备罐,14.药剂输送泵,14a.第一阀门,15.加药罐,16.计量泵,16a.第二阀门,17.第三液位传感器,18.第四液位传感器,19.第二储备罐,20.加药泵,21.控制柜,22.微机管理控制系统。In the figure: 1. Frequency conversion seawater pump, 2. Electric water replenishment valve, 3. Seawater replenishment flow meter, 4. First liquid level sensor, 5. Reservoir, 6. Seawater circulation pump, 7. Seawater conductivity sensor, 8. Sewage electric valve, 9. Sewage flow meter, 10. Heat exchanger, 11. Seawater cooling tower, 12. Second liquid level sensor, 13. First storage tank, 14. Drug delivery pump, 14a. First valve, 15 .dosing tank, 16. metering pump, 16a. second valve, 17. third liquid level sensor, 18. fourth liquid level sensor, 19. second storage tank, 20. dosing pump, 21. control cabinet, 22. Microcomputer management control system.
图2是实施例1中海水循环冷却系统浓缩倍数的控制情况。Fig. 2 is the control situation of the concentration ratio of the seawater circulating cooling system in embodiment 1.
图3是实施例1中海水阻垢缓蚀剂浓度随时间的变化。Fig. 3 is the variation of the concentration of seawater scale and corrosion inhibitors with time in Example 1.
具体实施方式detailed description
本实用新型是鉴于现有技术中在淡水循环冷却系统水处理管理控制方面的技术应用已基本成熟,但海水冷却系统中的应用报道较少,本发明人经过锐意研究后提供了本实用新型,在一种优选的实施方案中,其中海水循环冷却系统至少包括海水补水系统、循环水排污系统、加药系统、集水池、海水循环泵、热交换器、海水冷却塔。The utility model is based on the fact that the technical application in the water treatment management control of the fresh water circulation cooling system is basically mature in the prior art, but there are few application reports in the seawater cooling system. The inventor provides the utility model after diligent research. In a preferred embodiment, the seawater circulating cooling system at least includes a seawater replenishment system, a circulating water sewage system, a chemical dosing system, a sump, a seawater circulation pump, a heat exchanger, and a seawater cooling tower.
其中,补水系统由取水管线上的变频海水泵、补水电动阀、海水补水流量计、集水池中安装的液位传感器及管线组成,变频海水泵和补水电动阀与控制柜中PLC(可编程逻辑控制器)连接,海水补水流量计和液位传感器与控制柜中对应的流量和液位监测仪表连接,对应仪表再与PLC连接。Among them, the water replenishment system is composed of a frequency conversion seawater pump on the water intake pipeline, a water replenishment electric valve, a seawater replenishment flowmeter, a liquid level sensor installed in the sump, and a pipeline. The frequency conversion seawater pump, the water replenishment electric valve and the PLC (programmable logic controller), the seawater replenishment flowmeter and liquid level sensor are connected to the corresponding flow and liquid level monitoring instruments in the control cabinet, and the corresponding instruments are then connected to the PLC.
其中,循环水排污系统由在海水循环泵之后的回水支路安装的海水电导率传感器、排污支管线安装的排污电动阀、排污流量计及管线组成,排污电动阀与控制柜中PLC连接,海水电导率传感器和排污流量计与控制柜中对应的电导率和流量监测仪表连接,对应仪表再与PLC连接。Among them, the circulating water sewage system is composed of a seawater conductivity sensor installed in the return water branch after the seawater circulating pump, a sewage discharge electric valve installed in the sewage branch pipeline, a sewage discharge flowmeter and pipelines, and the sewage discharge electric valve is connected with the PLC in the control cabinet. The seawater conductivity sensor and the sewage flow meter are connected to the corresponding conductivity and flow monitoring instruments in the control cabinet, and the corresponding instruments are then connected to the PLC.
其中,加药系统包括海水阻垢缓蚀剂和海水菌藻抑制剂加药系统,海水阻垢缓蚀剂加药系统由储备罐及储备罐上安装的液位传感器、加药罐及加药罐上安装的计量泵和液位传感器及管线组成,药剂输送泵连接储备罐和加药罐,计量泵出口连接循环水回水支路,将药剂投加到集水池,计量泵与控制柜中PLC连接,液位传感器与控制柜中对应的液位监测仪表连接,对应仪表再与PLC连接;海水菌藻抑制剂加药系统由储备罐及第二储备罐上安装的液位传感器、加药泵及管线组成,加药泵连接储备罐将药剂通过加药管线直接投加到集水池中,加药泵与控制柜中PLC连接,液位传感器与控制柜中对应的液位监测仪表连接,对应仪表再与PLC连接。Among them, the dosing system includes the dosing system of seawater scale and corrosion inhibitors and seawater bacteria and algae inhibitors. The metering pump installed on the tank consists of a liquid level sensor and pipelines. The chemical delivery pump is connected to the storage tank and the dosing tank. The outlet of the metering pump is connected to the circulating water return branch, and the chemical is added to the sump, the metering pump and the control cabinet. PLC connection, the liquid level sensor is connected to the corresponding liquid level monitoring instrument in the control cabinet, and the corresponding instrument is connected to the PLC; Composed of pumps and pipelines, the dosing pump is connected to the storage tank to directly add the medicine to the sump through the dosing pipeline, the dosing pump is connected to the PLC in the control cabinet, and the liquid level sensor is connected to the corresponding liquid level monitoring instrument in the control cabinet. The corresponding instrument is then connected to the PLC.
海水循环冷却系统的水平衡和浓缩倍数通过调节海水补水量、集水池液位和排污水量控制,海水补水量通过液位传感器监测集水池液位,调节补水电动阀和变频海水泵;浓缩倍数通过监测循环水电导率、并辅以分析氯根计的浓缩倍数定期修正,设定对应控制浓缩倍数N(1.5~3.0)时的电导率为控制点,设置电导率变化区间为100~5000us/cm,优化为500~3000us/cm,自动控制排污电动阀,维持海水循环冷却系统的浓缩倍数在N±0.2条件下连续稳定运行。The water balance and concentration ratio of the seawater circulation cooling system are controlled by adjusting the seawater replenishment volume, the sump level and the sewage volume. Monitor the conductivity of the circulating water, supplemented by regular correction of the concentration ratio of the chlorine meter, set the conductivity corresponding to the control concentration ratio N (1.5~3.0) as the control point, and set the conductivity change range as 100~5000us/cm , optimized to 500-3000us/cm, automatic control of the sewage electric valve, maintaining the concentration multiple of the seawater circulating cooling system in continuous and stable operation under the condition of N±0.2.
海水水处理药剂的投加过程:海水阻垢缓蚀剂在基础投加开始浓缩运行时是通过液位传感器监测海水阻垢缓蚀剂储备罐的液位,控制药剂输送泵按系统容积成比例投加;海水菌藻抑制剂在基础投加开始浓缩运行时是通过液位传感器监测海水菌藻抑制剂储备罐的液位,控制加药泵按系统容积成比例投加;海水阻垢缓蚀剂在正常运行阶段是通过排污流量计计量循环水排污水量,控制计量泵按排污水量自动比例式投加;海水菌藻抑制剂在正常运行阶段是根据系统容积、加药周期(频率),每次投加浓度计算海水菌藻抑制剂的量,通过监测海水菌藻抑制剂储备罐的液位,控制加药泵自动投加。The dosing process of seawater treatment chemicals: when the seawater scale and corrosion inhibitors are concentrated and run after basic dosing, the liquid level of the seawater scale and corrosion inhibitor storage tanks is monitored by the liquid level sensor, and the chemical delivery pump is controlled in proportion to the system volume Dosing; seawater bacteria and algae inhibitors monitor the liquid level of the seawater bacteria and algae inhibitors storage tank through the liquid level sensor when the basic dosage starts to concentrate, and control the dosing pump to add in proportion to the system volume; seawater scale and corrosion inhibition In the normal operation stage, the agent is used to measure the sewage volume of circulating water by the sewage flowmeter, and the metering pump is controlled to automatically add proportionally according to the sewage volume; Calculate the amount of seawater algae inhibitor based on the concentration of each time, and control the automatic dosing of the dosing pump by monitoring the liquid level of the seawater algae inhibitor storage tank.
海水循环冷却系统水处理调控系统的微机管理控制系统通过总线与控制柜中的PLC连接,实现海水循环冷却系统水处理运行管理集成控制。The microcomputer management control system of the water treatment control system of the seawater circulation cooling system is connected with the PLC in the control cabinet through the bus to realize the integrated control of the water treatment operation management of the seawater circulation cooling system.
海水循环冷却系统水处理调控系统中所涉及的所有传感器、流量计、电动阀与海水、浓缩海水、药剂直接接触部件均选用耐海水腐蚀材料、耐酸碱材料,所述的药剂管线选用耐蚀非金属工程材料。All the sensors, flowmeters, electric valves involved in the water treatment control system of the seawater circulation cooling system, and the seawater, concentrated seawater, and components in direct contact with the chemicals are all made of seawater corrosion-resistant materials, acid and alkali resistant materials, and the chemical pipelines are made of corrosion-resistant materials. Non-metal engineering materials.
下面结合附图和各个实施例,对本实用新型及其有益技术效果进行详细说明。The utility model and its beneficial technical effects will be described in detail below in conjunction with the accompanying drawings and various embodiments.
实施例1Example 1
本实用新型的一种的优选实施方式中,包括下述结构:In a kind of preferred embodiment of the present utility model, comprise following structure:
如图1所示,海水循环冷却系统至少包括海水补水系统(1~4)、集水池5、海水循环泵6、热交换器10、海水冷却塔11、循环水排污系统(7~9)、加药系统(12~20)。As shown in Figure 1, the seawater circulation cooling system at least includes a seawater replenishment system (1-4), a sump 5, a seawater circulation pump 6, a heat exchanger 10, a seawater cooling tower 11, a circulating water sewage system (7-9), Dosing system (12-20).
如图1所示,补水系统包括取水管线上的变频海水泵1、补水电动阀2、海水补水流量计3、集水池5中安装的第一液位传感器4及管线,变频海水泵1和补水电动阀2与控制柜21中PLC连接,海水补水流量计3和第一液位传感器4与控制柜21中对应的流量和液位监测仪表连接,对应仪表再与PLC连接,PLC通过总线与微机管理控制系统22连接,海水补水量通过第一液位传感器4监测集水池5液位,调节控制补水电动阀2和变频海水泵1。As shown in Figure 1, the water replenishment system includes a frequency conversion seawater pump 1 on the water intake pipeline, a water replenishment electric valve 2, a seawater replenishment flow meter 3, a first liquid level sensor 4 installed in the sump 5 and pipelines, a frequency conversion seawater pump 1 and water replenishment The electric valve 2 is connected to the PLC in the control cabinet 21, the sea water replenishment flowmeter 3 and the first liquid level sensor 4 are connected to the corresponding flow and liquid level monitoring instruments in the control cabinet 21, and the corresponding instruments are connected to the PLC, and the PLC communicates with the microcomputer through the bus The management and control system 22 is connected, and the amount of seawater replenishment is monitored by the first liquid level sensor 4 to monitor the liquid level of the sump 5, and the electric valve 2 and the frequency conversion seawater pump 1 are adjusted and controlled.
如图1所示,循环水排污系统包括在海水循环泵6之后的回水支路安装的海水电导率传感器7、排污支管线安装的排污电动阀8、排污流量计9及管线,排污电动阀8与控制柜21中PLC连接,海水电导率传感器7和排污流量计9与控制柜21中对应的电导率和流量监测仪表连接,对应仪表再与PLC连接,PLC通过总线与微机管理控制系统22连接,浓缩倍数通过监测循环水电导率、并辅以分析氯根计的浓缩倍数定期修正,如设定对应控制浓缩倍数N=2.0时的电导率60000us/cm为控制点,设置电导率变化区间为2000us/cm,当循环水电导率超过60000us/cm时排污电动阀8自动打开,当循环水电导率低于58000us/cm时排污电动阀8自动关闭,维持海水循环冷却系统的浓缩倍数在2±0.2条件下连续稳定运行。As shown in Figure 1, the circulating water sewage system includes a seawater conductivity sensor 7 installed in the backwater branch after the seawater circulating pump 6, a sewage electric valve 8 installed in the sewage branch line, a sewage flow meter 9 and pipelines, and the sewage electric valve 8 is connected to the PLC in the control cabinet 21, the seawater conductivity sensor 7 and the sewage flowmeter 9 are connected to the corresponding conductivity and flow monitoring instruments in the control cabinet 21, and the corresponding instruments are connected to the PLC, and the PLC manages the control system 22 through the bus and the microcomputer Connection, the concentration ratio is regularly corrected by monitoring the conductivity of the circulating water and supplemented by the analysis of the concentration ratio of the chlorine meter, such as setting the conductivity 60000us/cm corresponding to the control concentration ratio N=2.0 as the control point, and setting the conductivity change interval 2000us/cm, when the conductivity of the circulating water exceeds 60000us/cm, the sewage electric valve 8 is automatically opened, and when the conductivity of the circulating water is lower than 58000us/cm, the sewage electric valve 8 is automatically closed, and the concentration factor of the seawater circulation cooling system is maintained at 2 Continuous and stable operation under the condition of ±0.2.
如图1所示,海水阻垢缓蚀剂加药系统包括第一储备罐13、第一储备罐13上安装的第二液位传感器12、加药罐15、加药罐15上安装的计量泵16和第三液位传感器17及管线,药剂输送泵14连接第一储备罐13和加药罐15,计量泵16出口连接循环水回水支路,将药剂投加到集水池5,计量泵16与控制柜21中PLC连接,第二液位传感器12和第三液位传感器17与控制柜21中对应的液位监测仪表连接,对应仪表再与PLC连接,PLC通过总线与微机管理控制系统22连接;海水菌藻抑制剂加药系统包括第二储备罐19、第二储备罐19上安装的第四液位传感器18、加药泵20及管线,加药泵20连接第二储备罐19将药剂通过加药管线直接投加到集水池5中,加药泵20与控制柜21中PLC连接,第四液位传感器18与控制柜21中对应的液位监测仪表连接,对应仪表再与PLC连接,PLC通过总线与微机管理控制系统22连接。海水水处理药剂的投加过程:As shown in Figure 1, the seawater scale and corrosion inhibitor dosing system includes a first storage tank 13, a second liquid level sensor 12 installed on the first storage tank 13, a dosing tank 15, and a metering device installed on the dosing tank 15. The pump 16, the third liquid level sensor 17 and the pipeline, the medicament delivery pump 14 is connected to the first storage tank 13 and the dosing tank 15, the outlet of the metering pump 16 is connected to the circulating water return branch, and the medicament is added to the sump 5 for metering. The pump 16 is connected to the PLC in the control cabinet 21, the second liquid level sensor 12 and the third liquid level sensor 17 are connected to the corresponding liquid level monitoring instruments in the control cabinet 21, and the corresponding instruments are connected to the PLC, and the PLC is managed and controlled by the microcomputer through the bus The system 22 is connected; the seawater bacteria and algae inhibitor dosing system includes the second storage tank 19, the fourth liquid level sensor 18 installed on the second storage tank 19, the dosing pump 20 and the pipeline, and the dosing pump 20 is connected to the second storage tank 19. Dosing the medicament directly into the sump 5 through the dosing pipeline, the dosing pump 20 is connected to the PLC in the control cabinet 21, the fourth liquid level sensor 18 is connected to the corresponding liquid level monitoring instrument in the control cabinet 21, and the corresponding instrument is then Connect with PLC, PLC is connected with microcomputer management control system 22 through bus line. Dosing process of sea water treatment chemicals:
如图1所示,海水阻垢缓蚀剂在基础投加开始浓缩运行时是通过第二液位传感器12监测药剂第一储备罐13的液位,控制药剂输送泵14,按系统容积成比例投加;海水菌藻抑制剂在基础投加开始浓缩运行时是通过第四液位传感器18监测药剂第二储备罐19的液位,控制加药泵20,按系统容积成比例投加;海水阻垢缓蚀剂在正常运行阶段是通过排污流量计9计量循环水排污水量,控制计量泵16,按排污水量自动比例式投加;海水菌藻抑制剂在正常运行阶段是根据系统容积、加药周期(频率),每次投加浓度计算海水菌藻抑制剂的量,通过监测药剂第二储备罐19的液位,控制加药泵20自动投加。其中监测药剂液位与海水阻垢缓蚀剂或菌藻抑制剂投加药剂量的关系为:药剂投加量=投加前后储备罐液位差×储备罐截面积×药剂密度。As shown in Figure 1, when the seawater scale and corrosion inhibitors start concentrated operation after basic dosing, the liquid level of the first chemical storage tank 13 is monitored by the second liquid level sensor 12, and the chemical delivery pump 14 is controlled, which is proportional to the system volume Dosing; when the seawater bacteria and algae inhibitor starts to concentrate and run after the basic dosing, the liquid level of the second storage tank 19 of the agent is monitored through the fourth liquid level sensor 18, and the dosing pump 20 is controlled to dosing in proportion to the system volume; seawater During the normal operation stage, the scale and corrosion inhibitors measure the sewage volume of circulating water through the sewage discharge flow meter 9, control the metering pump 16, and automatically add proportionally according to the sewage volume; The drug cycle (frequency), the amount of seawater bacteria and algae inhibitors are calculated each time the concentration is added, and the drug dosing pump 20 is controlled to automatically add the drug by monitoring the liquid level of the second storage tank 19 of the drug. The relationship between the liquid level of the monitoring agent and the dosage of seawater scale and corrosion inhibitors or algae inhibitors is as follows: Dosing amount of agent = liquid level difference of storage tank before and after adding × cross-sectional area of storage tank × agent density.
如图1所示,海水循环冷却系统水处理管理控制系统中所有选用的传感器、流量计、电动阀与海水、浓缩海水、药剂直接接触部件均选用耐海水腐蚀材料、耐酸碱材料,如特种不锈钢、钛合金、聚四氟等,所述的药剂管线选用耐蚀非金属工程材料,如ABS、PVC、UPVC等工程塑料。As shown in Figure 1, all the sensors, flow meters, electric valves used in the water treatment management and control system of the seawater circulation cooling system are in direct contact with seawater, concentrated seawater, and chemicals. Stainless steel, titanium alloy, polytetrafluoroethylene, etc., and the chemical pipeline is made of corrosion-resistant non-metallic engineering materials, such as ABS, PVC, UPVC and other engineering plastics.
工程实施例Engineering Example
以下结合我国首例化工行业天津塘沽海水循环冷却工程实例更进一步说明本实用新型。The utility model is further illustrated below in conjunction with the example of my country's first chemical industry Tianjin Tanggu seawater circulation cooling project.
(1)海水循环冷却系统水量平衡控制参数(1) Water balance control parameters of seawater circulating cooling system
海水循环水量2500m3/h,系统容积800m3,浓缩倍率控制2.0,蒸发损失约40m3/h,排污损失约40m3/h,补充水量约80m3/h,风吹损失忽略不计。The seawater circulating water volume is 2500m 3 /h, the system volume is 800m 3 , the concentration ratio is controlled at 2.0, the evaporation loss is about 40m 3 /h, the sewage loss is about 40m 3 /h, the supplementary water volume is about 80m 3 /h, and the wind blowing loss is negligible.
(2)海水循环冷系统调控方式(2) Control mode of seawater circulation cooling system
补水系统监测集水池液位,高低位报警控制;排污系统监测循环水电导率自动控制电动阀开关;加药系统监测排污水量按比例自动投加阻垢缓蚀剂;菌藻抑制剂按系统容积每3天冲击式间歇自动投加。The water supply system monitors the water level of the sump, and the high and low level alarm control; the sewage system monitors the conductivity of the circulating water and automatically controls the electric valve switch; the dosing system monitors the sewage volume and automatically adds scale and corrosion inhibitors in proportion; the bacteria and algae inhibitors are based on the volume of the system Intermittent automatic dosing every 3 days.
(3)海水循环冷却系统工艺正常控制指标(3) Process normal control index of seawater circulating cooling system
浓缩倍数2±0.2,电导率5万~6万us/cm(表显),排污电导率设置区间差100~300us/cm,流量变送器输出频率1次/10L~20L排污水,计量泵冲程、速度设置40%~80%。The concentration factor is 2±0.2, the conductivity is 50,000-60,000 us/cm (display), the sewage conductivity setting interval difference is 100-300us/cm, the output frequency of the flow transmitter is 1 time/10L-20L sewage, and the metering pump Stroke and speed are set at 40% to 80%.
(4)海水循环冷却系统水处理运行情况(4) Operation of water treatment in the seawater circulation cooling system
本海水循环冷却工程浓缩倍数的控制,主要通过连续监测系统循环水电导率,同时利用随机分析检测氯根的方法,修正电导率仪报警设置点(排污点)和报警区间(电导率控制区间差),控制电动阀自动开启或关闭,以实现维持系统浓缩倍数稳定运行,并结合补水控制和排污控制实现水平衡控制。The control of the concentration multiple of this seawater circulating cooling project is mainly through the continuous monitoring of the conductivity of the circulating water in the system, and at the same time, the method of random analysis and detection of chlorine radicals is used to correct the conductivity meter alarm setting point (pollution discharge point) and alarm interval (difference in the conductivity control interval) ), control the automatic opening or closing of the electric valve to maintain the stable operation of the system concentration multiple, and realize water balance control in combination with water replenishment control and sewage discharge control.
本海水循环冷却工程是由原淡水循环冷却系统成功切换到海水循环冷却系统,试验过程中连续检监测近100天的现场试验结果如图2所示。为保证系统的安全运行,根据现场情况,在浓缩运行初期控制浓缩倍数缓慢上升,经过一周的低浓缩倍数运行后过渡到正常运行。现场运行结果表明,本海水循环冷却工程,系统浓缩倍数控制稳定,基本维持在1.8~2.2,电导率维持在55000us/cm上下(表显),控制在预计范围5.0万~6.0万us/cm内,排污电导率设置区间差为100~200us/cm,也在预计范围100~300us/cm内。运行结果也进一步表明,采用连续监测循环水电导率,通过实现自动排污,控制系统浓缩倍数是有效可行的,为系统安全稳定运行,提供了强有力的保证。The seawater circulating cooling project was successfully switched from the original fresh water circulating cooling system to the seawater circulating cooling system. The field test results of continuous inspection and monitoring for nearly 100 days during the test are shown in Figure 2. In order to ensure the safe operation of the system, according to the site conditions, the concentration ratio is controlled to increase slowly at the initial stage of the concentration operation, and then transition to normal operation after a week of low concentration ratio operation. The field operation results show that the concentration ratio of the system in this seawater circulation cooling project is stable, basically maintained at 1.8-2.2, and the electrical conductivity is maintained at around 55000us/cm (shown), which is controlled within the expected range of 50,000-60,000us/cm , The sewage conductivity setting interval difference is 100-200us/cm, which is also within the expected range of 100-300us/cm. The operation results further show that it is effective and feasible to continuously monitor the conductivity of circulating water, realize automatic sewage discharge, and control the concentration multiple of the system, which provides a strong guarantee for the safe and stable operation of the system.
海水化学水处理是海水循环冷却技术的关键核心技术,主要是解决系统中的腐蚀、结垢和污损生物附着等问题。“三分药剂七分管理”,可见先进的系统调控技术是保证水处理效果的重要保证。本海水循环冷却自动加药系统,按排污水量成比例投加水处理药剂,维持系统正常药剂浓度,满足实际运行要求,试验过程中连续检监测近100天的现场试验结果如图3所示。按照预期制定的试验研究方案,系统进入浓缩运行阶段,阻垢缓蚀剂采用高剂量运行约10天,当浓缩倍数到达2.0左右时,进入正常运行阶段。根据现场实际运行情况,不同时期各药剂的控制指标做了相应的调整,但加药按排污水成比例投加,因此药剂浓度始终与控制指标较为接近。Seawater chemical water treatment is the key core technology of seawater circulating cooling technology, mainly to solve the problems of corrosion, scaling and fouling organisms in the system. "Three points of medicine and seven points of management", it can be seen that advanced system regulation technology is an important guarantee to ensure the effect of water treatment. In this seawater circulation cooling automatic dosing system, water treatment chemicals are added in proportion to the amount of sewage to maintain the normal concentration of the system and meet the actual operation requirements. The field test results of continuous monitoring for nearly 100 days during the test are shown in Figure 3. According to the experimental research plan formulated as expected, the system enters the concentrated operation stage, and the scale and corrosion inhibitors are operated for about 10 days at a high dose. When the concentration ratio reaches about 2.0, it enters the normal operation stage. According to the actual operation situation on site, the control indicators of each chemical agent have been adjusted accordingly in different periods, but the chemical dosing is added in proportion to the sewage, so the chemical concentration is always close to the control index.
(5)海水循环冷却系统水处理运行效果:(5) Water treatment operation effect of seawater circulating cooling system:
碳钢腐蚀控制:33天试片的平均腐蚀速率0.0331mm/a,83天试片的平均腐蚀速率0.0197mm/a,83天试验管的平均腐蚀速率0.0188mm/a;Carbon steel corrosion control: the average corrosion rate of the 33-day test piece is 0.0331mm/a, the average corrosion rate of the 83-day test piece is 0.0197mm/a, and the average corrosion rate of the 83-day test tube is 0.0188mm/a;
海水结垢控制:监测换热器测试年污垢热阻约为1.5×10-4m2K/W,83天粘附速度测定值为10.59mcm,属评价级别中“很好”范围;Scaling control in sea water: The thermal resistance of fouling in the year of monitoring heat exchanger test is about 1.5×10-4m 2 K/W, and the measured value of adhesion speed in 83 days is 10.59mcm, which belongs to the "very good" range in the evaluation level;
海水菌藻控制:异养菌菌数<5×105cfu/mL(夏季)、<1×105cfu/mL(冬季),铁细菌菌数<300cfu/mL,硫酸盐还原菌菌数<100cfu/mL。Seawater bacteria and algae control: the number of heterotrophic bacteria <5×10 5 cfu/mL (summer), <1×10 5 cfu/mL (winter), the number of iron bacteria <300cfu/mL, the number of sulfate-reducing bacteria < 100cfu/mL.
显然,海水循环冷却水处理运行效果良好,海水腐蚀、结垢、菌藻控制的各项指标均达到《海水循环冷却水处理设计规范》(GB/T 23248-2009)规定的技术指标,突破了淡水循环冷却系统要求的《工业循环冷却水处理设计规范》(GB 50050-2007)水质标准要求禁区,在我国实现了以海水替代淡水作为工业循环冷却水的技术创新。Obviously, the seawater circulating cooling water treatment has a good operation effect, and the indicators of seawater corrosion, scaling, and bacteria and algae control have all reached the technical indicators specified in the "Code for Design of Seawater Circulating Cooling Water Treatment" (GB/T 23248-2009), a breakthrough The "Code for Design of Industrial Circulating Cooling Water Treatment" (GB 50050-2007) water quality standard required by the fresh water circulating cooling system requires restricted areas. In my country, the technological innovation of replacing fresh water with seawater as industrial circulating cooling water has been realized.
以上是结合图1和工程实施例对本实用新型进行了详细描述,但本实用新型并不局限于上述的具体实施方式,上述的具体实施方式仅仅是示意性的,而不是限制性的,本领域的普通技术人员在本实用新型的启示下,在不脱离本实用新型宗旨的情况下,还可以作出很多变形,这些均属于本实用新型的保护范围之内。The above is a detailed description of the utility model in conjunction with Fig. 1 and engineering examples, but the utility model is not limited to the above-mentioned specific implementation, and the above-mentioned specific implementation is only illustrative, rather than restrictive. Under the enlightenment of the utility model, those skilled in the art can also make many deformations without departing from the gist of the utility model, and these all belong to the protection scope of the utility model.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107473299A (en) * | 2017-09-29 | 2017-12-15 | 四川德胜集团钒钛有限公司 | A kind of Metallurgical Waste Water frequency conversion circulatory system |
CN114956223A (en) * | 2021-09-14 | 2022-08-30 | 深圳市图灵科创产业发展有限公司 | Seawater concentration and desalination treatment system and treatment control method |
CN115432793A (en) * | 2022-10-08 | 2022-12-06 | 润电能源科学技术有限公司 | Automatic adjustment control system, method, equipment and medium for flocculant addition amount |
CN116300556A (en) * | 2022-11-24 | 2023-06-23 | 吕凡凡 | Circulating cooling water on-line monitoring control system and method |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN107473299A (en) * | 2017-09-29 | 2017-12-15 | 四川德胜集团钒钛有限公司 | A kind of Metallurgical Waste Water frequency conversion circulatory system |
CN114956223A (en) * | 2021-09-14 | 2022-08-30 | 深圳市图灵科创产业发展有限公司 | Seawater concentration and desalination treatment system and treatment control method |
CN115432793A (en) * | 2022-10-08 | 2022-12-06 | 润电能源科学技术有限公司 | Automatic adjustment control system, method, equipment and medium for flocculant addition amount |
CN116300556A (en) * | 2022-11-24 | 2023-06-23 | 吕凡凡 | Circulating cooling water on-line monitoring control system and method |
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