CN103060818A - Full-automatic control-corrosion system and application method of solar-energy hot-water storage tank - Google Patents
Full-automatic control-corrosion system and application method of solar-energy hot-water storage tank Download PDFInfo
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- 238000012360 testing method Methods 0.000 claims description 13
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- 229910052751 metal Inorganic materials 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract description 3
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- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
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- 229910052782 aluminium Inorganic materials 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
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Abstract
本发明涉及金属防腐技术领域,特别涉及一种太阳能热水储罐全自动腐蚀控制系统及其使用方法。该系统包括发生电流组件(1)、辅助阳极(8)和电缆线(10),其中,热水储罐(3)的外壁设置有阴极罐体电连接端子(9),内壁设置有辅助阳极(8),阴极罐体电连接端子(9)和辅助阳极(8)分别与发生电流组件(1)电连接;所述发生电流组件(1)的一侧设置有与之电连接的积分控制电路(2);所述热水储罐的内壁还设置有与积分控制电路(2)电连接的液面高度传感器(4)和温度传感器(7)。本发明结构简单,使用方便,造价低,控制方便,能根据热水储罐内腐蚀介质的温度和液面高度自动调节输出电流,使热水储罐随时处于被保护状态。
The invention relates to the technical field of metal anticorrosion, in particular to a fully automatic corrosion control system for a solar hot water storage tank and a method for using the same. The system includes a current generating component (1), an auxiliary anode (8) and a cable (10), wherein the outer wall of the hot water storage tank (3) is provided with a cathode tank electrical connection terminal (9), and the inner wall is provided with an auxiliary anode (8), the cathode tank electrical connection terminal (9) and the auxiliary anode (8) are respectively electrically connected to the generating current component (1); one side of the generating current component (1) is provided with an integral control unit electrically connected thereto Circuit (2); the inner wall of the hot water storage tank is also provided with a liquid level sensor (4) and a temperature sensor (7) electrically connected to the integral control circuit (2). The invention has the advantages of simple structure, convenient use, low cost and convenient control, and can automatically adjust the output current according to the temperature and liquid level of the corrosive medium in the hot water storage tank, so that the hot water storage tank is in a protected state at any time.
Description
技术领域technical field
本发明涉及金属防腐技术领域,特别涉及一种太阳能热水储罐全自动腐蚀控制系统及其使用方法。The invention relates to the technical field of metal anticorrosion, in particular to a fully automatic corrosion control system for a solar hot water storage tank and a method for using the same.
背景技术Background technique
将大量的单套太阳能集热器组合起来,组成一个大型的太阳能热水系统,为酒店、医院、学校、宾馆、高档小区等提供集体供应热水。太阳能热水储罐用于存储集热器出来的热水和补充的低温自来水或地下水,是该系统的一个重要组成部分。尽管常规淡水环境中钢结构腐蚀较轻,但储罐水介质高温时达到80~90℃,上水时低温0~10℃,罐内长期高低温交替,加速了罐体的腐蚀;加上地下水的含盐量高,腐蚀性强,罐壁腐蚀穿孔时有发生。Combine a large number of single sets of solar collectors to form a large-scale solar water heating system to provide collective hot water supply for hotels, hospitals, schools, guesthouses, and high-end residential areas. The solar hot water storage tank is used to store the hot water from the collector and the supplementary low-temperature tap water or ground water, which is an important part of the system. Although the corrosion of steel structures in the conventional fresh water environment is relatively light, the high temperature of the water medium in the storage tank reaches 80-90 °C, and the low temperature is 0-10 °C when the water is supplied. The long-term high and low temperature alternation in the tank accelerates the corrosion of the tank body; The salt content of the tank is high, the corrosion is strong, and the corrosion and perforation of the tank wall occur from time to time.
热水储罐的腐蚀防护技术包括牺牲阳极和外加电流法。由于罐内介质温度高,常规铝阳极和镁阳极消耗快,保护时间短,尤其是对于几十吨的大型储罐,需要安装大量的牺牲阳极,工程造价高。另外,长期饮用含有铝离子的水容易导致老年痴呆;而调查发现使用镁阳极溶解产物呈絮状,容易堵塞莲花喷头,在某些地区,水中含有大量SO42-、S2-,这些离子和镁等金属发生反应,形成H2S气体,产生臭鸡蛋味。外加电流法可分为恒电位法和恒电流法。恒电位法需要一个稳定的电极作为参比,通过施加一定的保护电流,使储罐内壁的钢结构极化到保护电位区间,但是到目前为止未发现能在此高温环境中长期使用的电位稳定的参比电极。恒电流法是通过向罐体提供一定的保护电流,使其极化到保护电位区间,关键技术是必须首先确定保护电流的大小。Corrosion protection techniques for hot water storage tanks include sacrificial anodes and impressed current methods. Due to the high temperature of the medium in the tank, the consumption of conventional aluminum and magnesium anodes is fast, and the protection time is short. Especially for large storage tanks of tens of tons, a large number of sacrificial anodes need to be installed, and the project cost is high. In addition, long-term drinking of water containing aluminum ions can easily lead to senile dementia; and the survey found that the dissolved products of magnesium anodes are flocculent, which is easy to block the lotus nozzle. In some areas, the water contains a lot of SO42-, S2-, these ions and magnesium, etc. The metal reacts to form H2S gas, which produces the smell of rotten eggs. Applied current method can be divided into constant potential method and constant current method. The constant potential method requires a stable electrode as a reference. By applying a certain protection current, the steel structure on the inner wall of the storage tank is polarized to the protection potential range. However, no stable potential that can be used in this high temperature environment for a long time has been found so far. the reference electrode. The constant current method is to provide a certain protection current to the tank to polarize it to the protection potential range. The key technology is to first determine the size of the protection current.
发明内容Contents of the invention
为解决上述技术问题,本发明的目的在于提供一种结构简单,使用方便,造价低,控制方便,能根据热水储罐内腐蚀介质的温度和液面高度自动调节输出电流的太阳能热水储罐全自动腐蚀控制系统及其使用方法。In order to solve the above technical problems, the object of the present invention is to provide a solar hot water storage system with simple structure, convenient use, low cost and convenient control, which can automatically adjust the output current according to the temperature and liquid level of the corrosive medium in the hot water storage tank. Fully automatic corrosion control system for tanks and method of use thereof.
为了实现上述目的,本发明提供了一种太阳能热水储罐全自动腐蚀控制系统,它包括发生电流组件1、辅助阳极8和电缆线10,其中,该热水储罐3的外壁设置有阴极罐体电连接端子9,热水储罐3的内壁设置有辅助阳极8,阴极罐体电连接端子9和辅助阳极8分别与发生电流组件1电连接;所述发生电流组件1的一侧设置有与之电连接的积分控制电路2;所述热水储罐的内壁还设置有与积分控制电路2电连接的液面高度传感器4和温度传感器7。In order to achieve the above purpose, the present invention provides a fully automatic corrosion control system for solar hot water storage tanks, which includes a
所述辅助阳极8数目为两个,一个固定设置在热水储罐3内壁的中上部,一个固定设置在热水储罐3内壁的中下部,两个辅助阳极8对向设置。The number of the
所述阴极罐体电连接端子9与所述发生电流组件1的负极通过电缆线10电连接;所述辅助阳极8通过电缆线10与发生电流组件1的正极电连接。The cathode tank
所述液面高度传感器4位于热水储罐3的出水口5的上方,液面高度传感器4的数目为多个,多个液面高度传感器4等距的固定安装在热水储罐3的内壁。The
所述温度传感器7位于热水储罐3的进水口6的上方,固定安装在热水储罐3内壁中下部的辅助阳极8的上方。The
为更好的实现本发明目的,本发明又提供了一种太阳能热水储罐全自动腐蚀控制系统的使用方法,其中,包括如下步骤:In order to better achieve the purpose of the present invention, the present invention further provides a method for using a fully automatic corrosion control system for solar hot water storage tanks, which includes the following steps:
a.热水储罐3存储有一定温度的介质,接通外电源,打开发生电流组件1和积分控制电路2;a. The hot
b.温度传感器7自动感应介质温度,以测试热水储罐3在不同温度下的介质温度中的保护电流密度;b. The
c.液面高度传感器4自动感应介质液面高度,以测试不同液面高度时,热水储罐3内壁与介质接触的总面积;c. The
d.将b和c步骤中所得的两组测试结果信号传递给积分控制电路2;d. The two groups of test result signals gained in the b and c steps are delivered to the
e.积分控制电路2根据介质液面高度和介质温度自动换算成保护电流,将其反馈给发生电流组件发生电流组件1;e.
f.发生电流组件1根据指令在阴极罐体电连接端子9与辅助阳极8之间施加某一电流。f. The
其中,步骤b中:测试热水储罐(3)在存储介质中不同温度下的单位面积所需的保护电流密度,温度与单位面积保护电流近似等效函数关系为:It=a1+b1t,0≤t≤85℃;其中,Among them, in step b: test the protection current density per unit area required by the hot water storage tank (3) at different temperatures in the storage medium, the approximate equivalent function relationship between temperature and unit area protection current is: I t =a 1 + b 1 t, 0≤t≤85℃; where,
t为罐内水的温度,单位为℃;t is the temperature of the water in the tank, in °C;
a1为常数,a1大小等于t为零摄氏度时单位材料所需的保护电流密度;a 1 is a constant, and the size of a 1 is equal to the protection current density required by the unit material when t is zero degrees Celsius;
b1为比例常数,反映保护电流密度随温度变化的关系;b 1 is a proportional constant, reflecting the relationship between the protection current density and the temperature change;
It为单位面积储罐罐壁金属材料在不同温度下达到完全保护所需要的电流,单位:mA/cm2。I t is the electric current required for the complete protection of the metal material of the storage tank wall per unit area at different temperatures, unit: mA/cm 2 .
步骤c中,测试不同液面高度时,热水储罐(3)内壁与介质接触的总面积;液面高度与接触总面积近似等效函数关系为:Sh=a2+b2h,0≤h;其中,In step c, when testing different liquid level heights, the total area of the inner wall of the hot water storage tank (3) in contact with the medium; the approximate equivalent functional relationship between the liquid level height and the total contact area is: S h =a 2 +b 2 h, 0≤h; where,
h为液面高度,单位为cm;h is the height of the liquid level in cm;
a2为常数,a2大小等于h为零时的储罐罐底面积;a 2 is a constant, and the size of a 2 is equal to the tank bottom area when h is zero;
b2为比例常数,反映储罐内壁与水接触面积随液面高度的变化关系; b2 is a proportional constant, which reflects the relationship between the contact area between the inner wall of the storage tank and the water with the height of the liquid level;
Sh为不同液面高度下的储罐内壁与介质接触的总面积,单位为cm2。S h is the total area of the inner wall of the storage tank in contact with the medium at different liquid level heights, the unit is cm 2 .
步骤e中,积分控制电流换算公式为:In step e, the integral control current conversion formula is:
Ip=It×Sh=(a1+b1t)×(Sh=a2+b2h)I p =I t ×S h =(a 1 +b 1 t)×(S h =a 2 +b 2 h)
其中Ip为不同温度不同液面高度下储罐内壁达到完全保护所需的保护电流。Among them, I p is the protection current required for complete protection of the inner wall of the storage tank at different temperatures and different liquid level heights.
本发明的优点为:结构简单,使用方便,造价低,控制方便,能根据热水储罐内腐蚀介质的温度和液面高度自动调节输出电流,使储罐内壁一直处于全面腐蚀控制状态。The invention has the advantages of simple structure, convenient use, low cost and convenient control, and can automatically adjust the output current according to the temperature and liquid level of the corrosive medium in the hot water storage tank, so that the inner wall of the storage tank is always in a state of comprehensive corrosion control.
附图说明Description of drawings
图1为本发明的全自动腐蚀控制系统的安装状态示意图。Fig. 1 is a schematic diagram of the installation state of the fully automatic corrosion control system of the present invention.
【主要组件符号说明】[Description of main component symbols]
1 发生电流组件1 Generating current component
2 积分控制电路2 Integral control circuit
3 热水储罐3 hot water storage tanks
4 液面高度传感器4 Liquid level sensor
5 出水口5 water outlet
6 进水口6 water inlet
7 温度传感器7 temperature sensor
8 辅助阳极8 auxiliary anode
9 阴极罐体电连接端子9 Cathode tank electrical connection terminal
10 电缆线10 cables
具体实施方式Detailed ways
下面结合附图,对本发明的具体实施方式做进一步说明。The specific implementation manners of the present invention will be further described below in conjunction with the accompanying drawings.
本发明的太阳能热水储罐全自动腐蚀控制系统包括发生电流组件1、辅助阳极8和电缆线10,其中,热水储罐3的外壁设置有阴极罐体电连接端子9,热水储罐3的内壁设置有辅助阳极8,阴极罐体电连接端子9与发生电流组件1的负极通过电缆线10电连接;辅助阳极8通过电缆线10与发生电流组件1的正极电连接;所述发生电流组件1的一侧进一步设置有积分控制电路2,发生电流组件1与积分控制电路2通过电缆线10电连接。The automatic corrosion control system for solar hot water storage tanks of the present invention includes a
本实施例中,所述辅助阳极8数目为两个,一个固定设置在热水储罐3内壁的中上部,一个固定设置在热水储罐3内壁的中下部,两个辅助阳极8对向设置。In this embodiment, the number of
所述热水储罐的内壁还设置有液面高度传感器4和温度传感器7,其中,液面高度传感器4位于热水储罐3的出水口5的上方,液面高度传感器4的数目为多个,多个液面高度传感器4等距的固定安装在热水储罐3的内壁,多个液面高度传感器4与积分控制电路2之间通过电缆线10电连接;温度传感器7位于热水储罐3的进水口6的上方,固定安装在热水储罐3内壁中下部的辅助阳极8的上方,温度传感器7与积分控制电路2之间通过电缆线10电连接。The inner wall of the hot water storage tank is also provided with a
其中,所述发生电流组件1是将220V家用交流电变压整流器转换为低压直流电并可调节输出电流。发生电流组件1的输入端为家用220V交流电(必要时也可采用低压直流电源替代),输出正极接辅助阳极8(通常为金属氧化物阳极,为了使罐体电流分布均匀,可在罐体内部同时安装多个辅助阳极),负极接罐体。Wherein, the
所述积分控制电路2主要用于波形变换、放大电路失调电压的消除及反馈控制中的积分补偿等场合。The
本发明的太阳能热水储罐全自动腐蚀控制系统的工作原理是:实验室内测试并确定储罐钢在存储的自来水(亦可能其他水源,本申请中假定为自来水)中不同温度下的单位面积所需的保护电流密度,将温度与单位面积保护电流近似等效成一函数关系;计算不同液面高度时储罐内壁与自来水接触的总面积,该液面高度与接水面积亦可近似为一函数关系。将上述两个近似函数式编程并存储到积分控制电路2中,至此只需知道罐内介质温度和液面高度,积分控制电路2将会根据水温和液面高度自动计算出所需的保护电流,同时反馈给发生电流组件1;具体为:The working principle of the automatic corrosion control system for solar hot water storage tanks of the present invention is to test and determine the units of storage tank steel at different temperatures in tap water (or other water sources, which are assumed to be tap water in this application) stored in the laboratory. The protective current density required by the area, the temperature and the protective current per unit area are approximately equivalent to a functional relationship; when calculating the total area of the tank inner wall in contact with tap water at different liquid level heights, the liquid level height and the water receiving area can also be approximated as A functional relationship. The above two approximate functions are programmed and stored in the
温度和液面传高度传感器将储罐内自来水的温度和液面高度参数传递给积分控制电路,积分控制电路通过内部逻辑运算计算出需要施加的保护电流信号,并将该信号传递给发生电流组件,发生电流组件通过辅助阳极向罐体施加一定的保护电流使其极化到保护电位区间。The temperature and liquid level transmission height sensor transmits the temperature and liquid level parameters of the tap water in the storage tank to the integral control circuit, and the integral control circuit calculates the protection current signal to be applied through internal logic operations, and transmits the signal to the generating current component , the generating current component applies a certain protection current to the tank through the auxiliary anode to make it polarized to the protection potential range.
因此,本发明的太阳能热水储罐全自动腐蚀控制系统的使用方法,包括如下步骤:Therefore, the method for using the automatic corrosion control system for solar hot water storage tanks of the present invention comprises the following steps:
a.热水储罐3存储有一定温度的介质,接通外电源,打开发生电流组件1和积分控制电路2;a. The hot
b.温度传感器7自动感应介质温度,以测试热水储罐3在不同温度下的介质温度中的保护电流密度;b. The
c.液面高度传感器4自动感应介质液面高度,以测试不同液面高度时,热水储罐3内壁与介质接触的总面积;c. The
d.将b和c步骤中所得的两组测试结果信号传递给积分控制电路2;d. The two groups of test result signals gained in the b and c steps are delivered to the
e.积分控制电路2根据介质液面高度和介质温度自动换算成保护电流,将其反馈给发生电流组件发生电流组件1;e.
f.发生电流组件1根据指令在阴极罐体电连接端子9与辅助阳极8之间施加某一电流。f. The
上述步骤b中:热水储罐在存储的自来水中不同温度下的单位面积所需的保护电流密度,将温度与单位面积保护电流近似等效成一函数关系,具体函数为:It=a1+b1t,0≤t≤85℃.In the above step b: the protection current density per unit area required by the hot water storage tank at different temperatures in the stored tap water, the temperature and the protection current per unit area are approximately equivalent to a functional relationship, and the specific function is: I t = a 1 +b 1 t, 0≤t≤85℃.
其中,It为单位面积储罐罐壁金属材料在不同温度下达到完全保护所需要的电流,单位为:mA/cm2.Among them, I t is the current required by the metal material of the tank wall per unit area to achieve complete protection at different temperatures, and the unit is: mA/cm 2 .
a1和b1为常数,a1大小等于t为零时的单位材料所需的保护电流密度。b1为比例常数,反映保护电流密度随温度变化关系。t为罐内水的温度,单位为℃.a 1 and b 1 are constants, and the size of a 1 is equal to the protection current density required by the unit material when t is zero. b 1 is a proportionality constant, which reflects the relationship between the protection current density and the temperature change. t is the temperature of the water in the tank, in °C.
步骤c中,计算不同液面高度下储罐内壁与水接触面积,该液面高度与接触总面积近似等效为一函数关系,具体函数为:Sh=a2+b2h,0≤h.In step c, calculate the contact area between the inner wall of the storage tank and water at different liquid level heights. The liquid level height and the total contact area are approximately equivalent to a functional relationship, and the specific function is: S h =a 2 +b 2 h, 0≤ h.
其中,Sh为不同液面高度下的储罐内壁与水接触面积,单位为cm2,Among them, S h is the contact area between the inner wall of the storage tank and water at different liquid level heights, the unit is cm 2 ,
a2和b2为常数,a2大小等于h为零时的储罐罐底面积。b2为比例常数,反映储罐内壁与水接触面积随液面高度的变化关系。h为液面高度,单位为cm.a 2 and b 2 are constants, and a 2 is equal to the tank bottom area when h is zero. b 2 is a proportional constant, which reflects the relationship between the contact area between the inner wall of the storage tank and the water with the height of the liquid level. h is the height of the liquid surface in cm.
步骤e中,积分控制电流换算公式为:Ip=It×Sh=(a1+b1t)×(Sh=a2+b2h)In step e, the integral control current conversion formula is: I p =I t ×S h =(a 1 +b 1 t)×(S h =a 2 +b 2 h)
其中Ip为不同温度不同液面高度下储罐内壁达到完全保护所需的保护电流。Among them, I p is the protection current required for complete protection of the inner wall of the storage tank at different temperatures and different liquid level heights.
本发明的太阳能热水储罐全自动腐蚀控制系统的工作时:首先,接通外电源,打开发生电流组件1和积分控制电路2,热水储罐3存储有一定温度的介质,温度传感器7和液面高度传感器4自动感应水温和液面高度,并将信号指令传递给积分控制电路2,积分控制电路2换算后反馈信号给发生电流组件1,发生电流组件1根据指令在阴极罐体电连接端子9与辅助阳极8施加某一电流,使热水储罐罐体电位极化到保护电位区间,达到腐蚀控制效果。When the solar hot water storage tank automatic corrosion control system of the present invention works: first, connect the external power supply, open the generating
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CN113063518A (en) * | 2021-03-24 | 2021-07-02 | 山东特种设备检验检测集团有限公司 | Atmospheric storage tank bottom plate corrosion monitoring method based on optical fiber sensing |
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