CN206740328U - A kind of condenser of power plant leak detection system - Google Patents
A kind of condenser of power plant leak detection system Download PDFInfo
- Publication number
- CN206740328U CN206740328U CN201720431478.9U CN201720431478U CN206740328U CN 206740328 U CN206740328 U CN 206740328U CN 201720431478 U CN201720431478 U CN 201720431478U CN 206740328 U CN206740328 U CN 206740328U
- Authority
- CN
- China
- Prior art keywords
- condenser
- conductivity
- electrode
- leak detection
- processing unit
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
- 238000001514 detection method Methods 0.000 title claims abstract description 43
- 238000005259 measurement Methods 0.000 claims abstract description 22
- 238000007789 sealing Methods 0.000 claims abstract description 18
- 238000012545 processing Methods 0.000 claims abstract description 16
- 238000004891 communication Methods 0.000 claims description 4
- 239000000565 sealant Substances 0.000 claims description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000007788 liquid Substances 0.000 claims description 3
- 238000012360 testing method Methods 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims 2
- 239000000463 material Substances 0.000 claims 1
- 239000011435 rock Substances 0.000 claims 1
- 238000003745 diagnosis Methods 0.000 abstract description 3
- 238000012423 maintenance Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 34
- 238000005070 sampling Methods 0.000 description 12
- 150000002500 ions Chemical class 0.000 description 6
- 239000000498 cooling water Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000012864 cross contamination Methods 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- FKNQFGJONOIPTF-UHFFFAOYSA-N Sodium cation Chemical compound [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Examining Or Testing Airtightness (AREA)
Abstract
一种发电厂凝汽器泄漏检测系统,包括布置在凝汽器热井内的N 个电导率电极,电导率电极安装在电极密封座内,电导率电极的电极电缆通过电缆引出管引出,与电导率变送器连接,电导率变送器与中央处理器连接,将接收到的电导率电极测量信号传送给中央处理器,中央处理器与显示屏连接,将检测结果输出显示在显示屏上,所述电导率变送器、中央处理器和显示屏集中布置在凝汽器检漏柜内;本实用新型具有系统简单、测量准确、诊断可靠、维护量小等显著优点,为发电厂运行中处理凝汽器泄漏提供准确可靠的决策依据。
A condenser leakage detection system in a power plant, including N conductivity electrodes arranged in the hot well of the condenser, the conductivity electrodes are installed in the electrode sealing seat, the electrode cables of the conductivity electrodes are drawn out through the cable outlet pipe, and the conductivity electrodes are connected with the conductivity electrodes. The conductivity transmitter is connected to the central processing unit, and the received conductivity electrode measurement signal is transmitted to the central processing unit, and the central processing unit is connected to the display screen, and the detection result output is displayed on the display screen. The conductivity transmitter, central processing unit and display screen are centrally arranged in the condenser leak detection cabinet; the utility model has significant advantages such as simple system, accurate measurement, reliable diagnosis, and small maintenance amount, and is suitable for the operation of power plants. Dealing with condenser leakage provides accurate and reliable decision-making basis.
Description
技术领域technical field
本实用新型涉及发电技术领域,尤其涉及一种发电厂凝汽器泄漏检测系统。The utility model relates to the technical field of power generation, in particular to a leakage detection system for a condenser of a power plant.
背景技术Background technique
凝汽器换热管运行中泄漏是长期以来困扰发电厂安全运行的重要隐患之一,特别是海水冷却电厂。当凝汽器发生泄漏后,凝结水被污染,导致热力系统水汽品质迅速恶化,造成热力系统设备短时间内严重腐蚀结垢,威胁机组的安全运行,即使是装备有凝结水精除盐系统的机组,最多也只能坚持几个小时,如果在这几个小时之内不能找到泄漏位置并处理,就只能紧急停机查找漏点并处理。Leakage of condenser heat exchange tubes during operation is one of the important hidden dangers that have long plagued the safe operation of power plants, especially seawater cooling power plants. When the condenser leaks, the condensed water is polluted, leading to rapid deterioration of the water vapor quality in the thermal system, causing serious corrosion and fouling of the thermal system equipment in a short period of time, threatening the safe operation of the unit, even if it is equipped with a condensate desalination system The unit can only persist for a few hours at most. If the leak location cannot be found and treated within these few hours, it can only be shut down urgently to find the leak and deal with it.
由于凝汽器换热管内流动的冷却水杂质离子浓度远远高于凝汽器热井中蒸汽冷凝下来的凝结水,因此,凝汽器泄漏最显著的特征就是凝结水中的杂质离子浓度增加,杂质离子浓度增加的程度就表征了冷却水的泄漏程度。因此,检测凝结水中的杂质离子浓度是判断凝汽器是否泄漏、泄漏点位置及计算泄漏率的重要参数。Since the concentration of impurity ions in the cooling water flowing in the heat exchange tube of the condenser is much higher than that of the condensed water condensed from the steam in the hot well of the condenser, the most obvious feature of the leakage of the condenser is the increase of the concentration of impurity ions in the condensed water. The degree of increase in ion concentration characterizes the degree of leakage of cooling water. Therefore, detecting the concentration of impurity ions in condensed water is an important parameter for judging whether the condenser is leaking, the location of the leak point, and calculating the leak rate.
现有的凝汽器检漏技术的共同特点:1)在凝汽器热井内设置取样点,通过真空泵将凝结水抽取到凝汽器外;2)通过检测不同取样点水样的氢电导率或Na+浓度来判断泄漏区域。The common characteristics of the existing condenser leak detection technology: 1) Set sampling points in the hot well of the condenser, and pump the condensed water out of the condenser through a vacuum pump; 2) By detecting the hydrogen conductivity of water samples at different sampling points or Na + concentration to judge the leakage area.
现有凝汽器检漏装置存在的问题:1)取样代表性较差,目前的取样点均设置在每个水室的凝汽器两端,一种是在每个水室管束两端的集水槽内(只能检测凝汽器管口泄漏),一种是在靠近管束两端的热井液面下(只能检测管口及靠近管口的换热管泄漏);2)水样存在交叉污染。为了节省成本,一般的凝汽器检漏装置都是多个取样点(一般8个)公用1套(1用1备)取样泵和测量系统,这些取样点间隔一定的时间切换取样并测量水样中的杂质离子浓度,水样切换容易造成交叉污染;而且,每一个水样都是在不同时间点测定的,而其对泄漏点及泄漏量的判断是通过比较不同测点的离子浓度差别来确定的,因此,经常出现不容易确定泄漏点甚至判断错误的现象。3)经常抽不出水样。由于凝汽器在真空下运行,一般运行压力在4.9kPa(绝对压力)左右,真空度非常高,如果要连续稳定抽取水样,对取样泵以及取样管路、阀门、泵的安装高度等要求非常高,只要某一个环节出现问题,就抽不出水样。4)水样滞后时间较长。水样从凝汽器热井抽取到凝汽器检漏柜在线化学仪表要流经几十米的取样管路,需要消耗一定的时间,因此,必然存在水样滞后问题。如果要水样滞后时间短,取样流速就要高,但是流速一高,取样系统阻力就大,泵的抽吸能力达不到。Problems existing in the existing condenser leak detection device: 1) The sampling representativeness is poor. The current sampling points are all set at the two ends of the condenser in each water chamber. In the water tank (can only detect the leakage of the nozzle of the condenser), one is under the liquid surface of the hot well near the two ends of the tube bundle (only can detect the leakage of the nozzle and the heat exchange tube near the nozzle); 2) There is crossover in the water sample pollute. In order to save costs, the general condenser leak detection device uses multiple sampling points (generally 8) to share a set of sampling pumps and measurement systems (1 for use and 1 for standby). The concentration of impurity ions in the sample, water sample switching is likely to cause cross-contamination; moreover, each water sample is measured at different time points, and the judgment of the leakage point and leakage is by comparing the ion concentration difference of different measurement points Therefore, it is often difficult to determine the leakage point or even make a wrong judgment. 3) It is often impossible to draw water samples. Since the condenser operates under vacuum, the general operating pressure is about 4.9kPa (absolute pressure), and the vacuum degree is very high. If water samples are to be continuously and stably drawn, there are requirements for the installation height of the sampling pump, sampling pipeline, valves and pumps, etc. Very high, as long as there is a problem in a certain link, no water sample can be drawn. 4) The lag time of water samples is longer. It takes a certain amount of time for the water sample to be drawn from the hot well of the condenser to the online chemical instrument of the condenser leak detection cabinet through a sampling pipeline of tens of meters. Therefore, there must be a problem of water sample lag. If the lag time of the water sample is to be short, the sampling flow rate must be high, but if the flow rate is high, the resistance of the sampling system will be large, and the suction capacity of the pump cannot be reached.
由于现有的凝汽器检漏技术原理大同小异,固有的设计缺陷无法得到根本改善,因此,发电厂急需一种全新的能够快速准确地判断凝汽器运行中泄漏区域及泄漏量的检测技术。Since the existing condenser leak detection technology has similar principles and inherent design defects cannot be fundamentally improved, power plants urgently need a new detection technology that can quickly and accurately determine the leakage area and leakage volume of the condenser during operation.
实用新型内容Utility model content
本实用新型针对现有凝汽器检漏技术固有的问题,提供一种全新的能够快速准确检测发电厂凝汽器运行中泄漏的检测系统,可检测漏率达到0.0005%。The utility model aims at the inherent problems of the existing condenser leak detection technology, and provides a brand-new detection system capable of quickly and accurately detecting the leakage of the condenser in power plant operation, and the detectable leakage rate reaches 0.0005%.
为达到上述目的,本实用新型采用的技术方案如下:In order to achieve the above object, the technical scheme adopted by the utility model is as follows:
一种发电厂凝汽器泄漏检测系统,包括布置在凝汽器热井内的N个电导率电极2,电导率电极2安装在电极密封座1内,电导率电极2的电极电缆3通过电缆引出管4引出,与电导率变送器5连接,电导率变送器5与中央处理器6连接,将接收到的电导率电极2测量信号传送给中央处理器6,中央处理器6与显示屏7连接,将检测结果输出显示在显示屏7上,所述电导率变送器5、中央处理器6和显示屏7集中布置在凝汽器检漏柜8内。A condenser leakage detection system in a power plant, including N conductivity electrodes 2 arranged in the hot well of the condenser, the conductivity electrodes 2 are installed in the electrode sealing seat 1, and the electrode cables 3 of the conductivity electrodes 2 are led out through the cables The tube 4 leads out and is connected with the conductivity transmitter 5, and the conductivity transmitter 5 is connected with the central processing unit 6, and transmits the received measurement signal of the conductivity electrode 2 to the central processing unit 6, and the central processing unit 6 and the display screen 7 connection, the detection result output is displayed on the display screen 7, and the conductivity transmitter 5, the central processing unit 6 and the display screen 7 are collectively arranged in the condenser leak detection cabinet 8.
为确保测点的代表性和检漏装置的灵敏度,每个水室沿凝汽器管长度方向布置若干个所述电导率电极2,其测量部分浸没在凝汽器热井最低运行液面之下0‐500mm处,且电导率电极2均位于每个水室凝结水流动方向的下游靠近出水口,从而实现对每个凝汽器水室凝结水水质检测全覆盖;电导率电极2数量N根据凝汽器的大小和凝结水出水口的位置确定。In order to ensure the representativeness of the measuring points and the sensitivity of the leak detection device, several conductivity electrodes 2 are arranged along the length of the condenser tube in each water chamber, and the measuring part is immersed in the lowest operating liquid level of the hot well of the condenser 0-500mm below, and the conductivity electrode 2 is located downstream of the condensate flow direction of each water chamber and close to the water outlet, so as to achieve full coverage of the condensate water quality detection in each condenser water chamber; the number of conductivity electrodes 2 N Determined according to the size of the condenser and the location of the condensate outlet.
所述电极密封座1与电导率电极2采用螺纹连接,密封结构为“O”型圈密封结合加注密封剂密封,将电导率电极2密封在电极密封座1内;电极密封座1与电缆引出管4采用螺纹连接,密封结构为“O”型圈密封,将电极电缆3密封在电缆引出管4内。The electrode sealing seat 1 and the conductivity electrode 2 are connected by threads, and the sealing structure is an "O" ring seal combined with a sealant seal, so that the conductivity electrode 2 is sealed in the electrode sealing seat 1; the electrode sealing seat 1 and the cable The lead-out pipe 4 is connected by threads, and the sealing structure is an "O" ring seal, which seals the electrode cable 3 in the cable lead-out pipe 4 .
所述电缆引出管4材质为不锈钢,末端采用不锈钢堵头焊接密封,另一端穿过凝汽器侧壁,电缆引出管4与凝汽器侧壁相接处采用焊接密封。The cable outlet pipe 4 is made of stainless steel, and the end is welded and sealed with a stainless steel plug, and the other end passes through the side wall of the condenser, and the connection between the cable outlet pipe 4 and the side wall of the condenser is sealed by welding.
所述电缆引出管4焊接在凝汽器热井内部的钢支撑架上,确保电缆引出管在凝汽器运行中牢固、不晃动。The cable outlet pipe 4 is welded on the steel support frame inside the hot well of the condenser to ensure that the cable outlet pipe is firm and does not shake during the operation of the condenser.
所述中央处理器6配备无线通讯模块,能实现诊断结果的远程传输。The central processing unit 6 is equipped with a wireless communication module, which can realize remote transmission of diagnosis results.
本实用新型和现有技术相比具有以下优点。Compared with the prior art, the utility model has the following advantages.
1、本实用新型根据比电导率测定结果诊断凝汽器泄漏,而比电导率测量具有响应时间快、测量结果可靠性高,电极基本免维护的特点,从根本上解决了氢电导率测量需要考虑氢交换柱失效问题、响应时间慢;钠离子测量仪表维护工作量大、容易交叉污染、成本高的固有问题。1. The utility model diagnoses the leakage of the condenser according to the measurement results of the specific conductivity, and the measurement of the specific conductivity has the characteristics of fast response time, high reliability of the measurement results, and basically maintenance-free electrodes, which fundamentally solves the need for hydrogen conductivity measurement Consider the failure of the hydrogen exchange column, slow response time; the inherent problems of heavy maintenance workload, easy cross-contamination, and high cost of sodium ion measuring instruments.
2、由于电极直接布置在凝汽器热井内,因此,不存在水样滞后及水样交叉污染问题。2. Since the electrodes are directly arranged in the hot well of the condenser, there is no problem of water sample lag and water sample cross-contamination.
3、由于本实用新型是直接测定凝汽器热井内的凝结水,不需要将水样抽取到凝汽器外,因此,不需要真空泵、阀门、压力表及水样自动切换控制系统等,整个系统非常简单,运行中可以做到免维护,机组检修时,只需要对电极密封进行检查,对电极进行清洗即可。3. Since the utility model directly measures the condensed water in the hot well of the condenser, it does not need to extract the water sample out of the condenser. Therefore, it does not need a vacuum pump, valve, pressure gauge, and water sample automatic switching control system, etc., and the whole The system is very simple, and it can be maintenance-free during operation. When the unit is overhauled, it is only necessary to check the electrode seal and clean the electrode.
4、由于水样测点(一般32个)远远多于现有的检漏系统(一般8个取样点),因此,水样的代表性强,几乎没有盲区,而且所有的测点均是同时测量,不存在时间差,容易诊断泄漏区域,不会出现漏判、误判的现象。4. Since the water sample measuring points (generally 32) are far more than the existing leak detection system (generally 8 sampling points), the representativeness of the water sample is strong, there is almost no blind area, and all the measuring points are Simultaneous measurement, there is no time difference, easy to diagnose the leakage area, and there will be no missed or misjudged phenomena.
5、检测结果显示非常直观,泄漏点一目了然,不需要运行人员进行二次数据分析和判断;诊断结果非常全面,泄漏位置、泄漏率、泄漏率一应俱全,非常方面运行人员决策处理措施。5. The detection result is very intuitive, the leakage point is clear at a glance, and the operator does not need to conduct secondary data analysis and judgment; the diagnosis result is very comprehensive, and the leakage location, leakage rate, and leakage rate are all available, which is very convenient for the operator to decide and deal with.
6、具有远程监视功能,运行人员随时随地就可以掌握凝汽器泄漏检测结果。6. With the function of remote monitoring, the operating personnel can grasp the leakage detection results of the condenser anytime and anywhere.
附图说明Description of drawings
图1为凝汽器泄漏检测系统示意图。Figure 1 is a schematic diagram of the condenser leak detection system.
图2为凝汽器检漏装置整体示意图。Figure 2 is an overall schematic diagram of the condenser leak detection device.
图3为电导率率电极与电极密封座及电缆引出管连接方式。Figure 3 shows the connection method between the conductivity electrode, the electrode sealing seat and the cable outlet tube.
图4为凝汽器泄漏检测结果示意图,其中图4(a)案例1测定结果,其中图4(b)案例1测定结果。Figure 4 is a schematic diagram of the leak detection results of the condenser, where Figure 4(a) is the measurement result of Case 1, and Figure 4(b) is the measurement result of Case 1.
具体实施方式detailed description
下面结合附图对本实用新型作进一步详细说明。Below in conjunction with accompanying drawing, the utility model is described in further detail.
如图1,打开安装在凝汽器检漏柜8内的电导率变送器5电源开关,布置在凝汽器每个水室热井凝结水液面下的N个电导率电极2将测定的不同区域凝结水电导率信号(各测点电导率分别为K1,K2,…KN,其中测点最大电导率为Kmax,所有测点最小电导率Kmin)通过密封在电缆引出管4内的电极电缆3传送给电导率变送器5,电导率变送器5接受电导率测量信号后,传送给安装在凝汽器检漏柜8内的中央处理6,中央处理器6通过比较不同测点的电导率测定结果,当某个电导率电极测量的电导率值Kx与各测点的最小电导率值Kmin的差值超过设定范围时,即Kx‐Kmin>△K时,判定该测定位置发生泄漏。中央处理器通过比较泄漏区域电导率值Kx与未泄漏区域电导率值Kmin差值,结合凝汽器冷却水电导率K冷却水以及凝结水流量Vn,计算得到凝汽器泄漏率δ=[(Kx‐Kmin)/K冷却水],凝汽器泄漏量VL=1000×δ×Vn,并将泄漏位置、泄漏率、泄漏量显示在安装于凝汽器检漏柜8的显示屏7上,检测结果通过安装在无线通讯模块同步无线传输给安装有凝汽器检漏应用软件的运行人员的手机上,让运行人员随时随地掌握凝汽器检漏结果,实现远程监控。其中,电导率K单位为μS/cm,凝结水流量Vn单位为t/h,凝汽器泄漏率δ单位为%,凝汽器泄漏量VL单位为Kg/h。As shown in Figure 1, turn on the power switch of the conductivity transmitter 5 installed in the condenser leak detection cabinet 8, and the N conductivity electrodes 2 arranged under the condensed water level of each water chamber hot well of the condenser will measure Condensed water conductivity signals in different areas (the conductivity of each measuring point is K 1 , K 2 , ... K N , where the maximum conductivity of the measurement point is K max , and the minimum conductivity of all the measurement points is K min ) are drawn out through the sealed cable The electrode cable 3 in the tube 4 is sent to the conductivity transmitter 5, and the conductivity transmitter 5 receives the conductivity measurement signal, and then sends it to the central processing unit 6 installed in the condenser leak detection cabinet 8, and the central processing unit 6 By comparing the conductivity measurement results of different measuring points, when the difference between the conductivity value K x measured by a certain conductivity electrode and the minimum conductivity value K min of each measuring point exceeds the set range, that is, K x -K min >△K, it is determined that there is a leak at the measurement position. The central processor calculates the condenser leakage rate δ by comparing the difference between the conductivity value K x of the leakage area and the conductivity value K min of the non-leakage area, combined with the conductivity K cooling water of the condenser cooling water and the condensate flow rate V n =[(K x ‐K min )/K cooling water ], condenser leakage V L =1000×δ×V n , and display the leakage location, leakage rate and leakage amount on the leak detection cabinet installed in the condenser On the display screen 7 of 8, the detection results are synchronously and wirelessly transmitted to the mobile phones of the operators who have installed the condenser leak detection application software through the wireless communication module, so that the operators can grasp the condenser leak detection results anytime and anywhere, and realize remote control. monitor. Among them, the unit of conductivity K is μS/cm, the unit of condensate flow V n is t/h, the unit of condenser leakage rate δ is %, and the unit of condenser leakage V L is Kg/h.
为了使检测结果看起来更直观,检测结果按照电导率测点在凝汽器中的实际布置位置实时显示在检漏控制柜的显示屏上,电厂运行人员可以非常直观的掌握凝汽器热井每个测点测定结果。并且,诊断结果(泄漏位置、泄漏率、泄漏量)也显示在显示屏上,让运行人员一目了然。In order to make the test results look more intuitive, the test results are displayed on the display screen of the leak detection control cabinet in real time according to the actual arrangement position of the conductivity measuring point in the condenser, so that the power plant operators can intuitively grasp the hot well of the condenser The results of each measurement point. In addition, the diagnostic results (leakage location, leakage rate, and leakage volume) are also displayed on the display screen, so that operators can see at a glance.
为了实现远程监控,中央处理器配备有无线通讯模块,在电厂运行人员的手机上安装应用软件后,电厂运行人员可以随时随地通过手机了解凝汽器泄漏检测结果。In order to realize remote monitoring, the central processor is equipped with a wireless communication module. After installing the application software on the mobile phone of the power plant operator, the plant operator can know the condenser leakage detection results through the mobile phone anytime and anywhere.
凝汽器检漏装置整体示意图参见图2。The overall schematic diagram of the condenser leak detection device is shown in Figure 2.
为确保电导率测量系统的严密性(如果系统不严密将影响凝汽器的真空,甚至导致机组不能运行)以及电导率电极电缆线处于干燥环境(电缆线长期处于湿热环境中可能会导致电缆线损坏,导致电导率测量错误),安装时,先将电极尾部与电极密封座连接,然后将电极电缆线穿入电缆引出管,再将电极密封座与电缆引出管密封连接,将电极电缆线密封在电缆引出管内,从而确保测量系统的严密性。In order to ensure the tightness of the conductivity measurement system (if the system is not tight, it will affect the vacuum of the condenser, and even cause the unit to fail to operate) and the conductivity electrode cable is in a dry environment (the cable line in a humid and hot environment for a long time may cause the cable line to When installing, first connect the electrode tail to the electrode sealing seat, then pass the electrode cable into the cable lead-out tube, and then seal the electrode sealing seat to the cable lead-out tube to seal the electrode cable In the cable outlet tube, so as to ensure the tightness of the measurement system.
电导率率电极与电极密封座及电缆引出管连接方式参加图3,先将电导率电极2与电极密封座1采用螺纹连接,O型圈密封,然后向电极密封座内加注5cm左右高度的密封剂进一步密封;待密封剂固化后,将电极密封座1与电缆引出管4通过螺纹连接紧固,O型圈密封。Refer to Figure 3 for the connection method of the conductivity electrode, the electrode sealing seat and the cable outlet tube. Firstly, the conductivity electrode 2 and the electrode sealing seat 1 are connected by threads, sealed with an O-ring, and then filled into the electrode sealing seat with a height of about 5cm. The sealant is further sealed; after the sealant is cured, the electrode sealing seat 1 and the cable outlet pipe 4 are screwed and fastened, and the O-ring is sealed.
图4为凝汽器泄漏检测结果示意图。图(a)案例1为凝汽器未发生泄漏时的检测结果示例,图(b)案例2为凝汽器发生泄漏时的检测结果示例。Figure 4 is a schematic diagram of the leak detection results of the condenser. Figure (a) Case 1 is an example of the detection results when the condenser does not leak, and Figure (b) Case 2 is an example of the detection results when the condenser leaks.
Claims (6)
- A kind of 1. condenser of power plant leak detection system, it is characterised in that:Including the N number of conductance being arranged in condenser hotwell Rate electrode (2), conductivity electrode (2) are arranged in electrode seal receptacle (1), and the electrode cable (3) of conductivity electrode (2) passes through electricity Cable fairlead (4) is drawn, and is connected with conductivity transmitter (5), conductivity transmitter (5) is connected with central processing unit (6), will be connect Conductivity electrode (2) measurement signal received sends central processing unit (6) to, and central processing unit (6) is connected with display screen (7), By testing result output display on display screen (7), the conductivity transmitter (5), central processing unit (6) and display screen (7) Centralized arrangement is in condenser leakage detection cabinet (8).
- 2. condenser of power plant leak detection system according to claim 1, it is characterised in that:Each hydroecium is along condenser Several conductivity electrodes (2) are arranged in length of tube direction, and its measurement is partially immersed in condenser hotwell minimum operation liquid level Under at 0-500mm, and conductivity electrode (2) is respectively positioned on the downstream of each hydroecium condensate flow direction close to delivery port;Electricity Conductance electrode (2) quantity N determines according to the size of condenser and the position of condensate delivery port.
- 3. condenser of power plant leak detection system according to claim 1, it is characterised in that:Electrode seal receptacle (1) with Conductivity electrode (2) is using threaded connection, and sealing structure is that "O"-ring sealing combines filling sealant sealing, by electro conductivity Pole (2) is sealed in electrode seal receptacle (1);Electrode seal receptacle (1) is used with cable fairlead (4) and is threadedly coupled, sealing structure Sealed for "O"-ring, electrode cable (3) is sealed in cable fairlead (4).
- 4. condenser of power plant leak detection system according to claim 1, it is characterised in that:The cable fairlead (4) material is stainless steel, and end uses stainless steel plug welded seal, and the other end passes through condenser side wall, cable fairlead (4) Welded seal is used with condenser side wall joint.
- 5. condenser of power plant leak detection system according to claim 1, it is characterised in that:The cable fairlead (4) it is welded on the bracing members frame inside condenser hotwell, it is ensured that cable fairlead is firm in condenser operation, does not rock.
- 6. condenser of power plant leak detection system according to claim 1, it is characterised in that:The central processing unit (6) wireless communication module is equipped with, the remote transmission of diagnostic result can be realized.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720431478.9U CN206740328U (en) | 2017-04-21 | 2017-04-21 | A kind of condenser of power plant leak detection system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720431478.9U CN206740328U (en) | 2017-04-21 | 2017-04-21 | A kind of condenser of power plant leak detection system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206740328U true CN206740328U (en) | 2017-12-12 |
Family
ID=60561590
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720431478.9U Withdrawn - After Issue CN206740328U (en) | 2017-04-21 | 2017-04-21 | A kind of condenser of power plant leak detection system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206740328U (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106969885A (en) * | 2017-04-21 | 2017-07-21 | 西安热工研究院有限公司 | A kind of condenser of power plant leak detection system and detection method |
CN112902203A (en) * | 2021-03-05 | 2021-06-04 | 西安热工研究院有限公司 | Power station boiler steam soot blowing system and intelligent leakage detection identification method thereof |
CN114088303A (en) * | 2021-11-19 | 2022-02-25 | 西安热工研究院有限公司 | A system and method for locating the position of a condenser leaking heat exchange tube |
CN115420435A (en) * | 2022-08-31 | 2022-12-02 | 西安热工研究院有限公司 | Online leakage detection device and method for heat exchange tube of condenser of thermal power unit |
-
2017
- 2017-04-21 CN CN201720431478.9U patent/CN206740328U/en not_active Withdrawn - After Issue
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106969885A (en) * | 2017-04-21 | 2017-07-21 | 西安热工研究院有限公司 | A kind of condenser of power plant leak detection system and detection method |
CN112902203A (en) * | 2021-03-05 | 2021-06-04 | 西安热工研究院有限公司 | Power station boiler steam soot blowing system and intelligent leakage detection identification method thereof |
CN112902203B (en) * | 2021-03-05 | 2022-03-22 | 西安热工研究院有限公司 | Power station boiler steam soot blowing system and intelligent leakage detection identification method thereof |
CN114088303A (en) * | 2021-11-19 | 2022-02-25 | 西安热工研究院有限公司 | A system and method for locating the position of a condenser leaking heat exchange tube |
CN115420435A (en) * | 2022-08-31 | 2022-12-02 | 西安热工研究院有限公司 | Online leakage detection device and method for heat exchange tube of condenser of thermal power unit |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106969885B (en) | A leak detection system and detection method for a condenser in a power plant | |
CN206740328U (en) | A kind of condenser of power plant leak detection system | |
CN205607831U (en) | Online inductance probe corrosion monitoring system | |
CN102182929A (en) | Device and method for detecting pipeline blockage | |
CN101666784A (en) | Chromatographic instrument calibration device | |
CN111239573A (en) | A kind of online diagnosis method and device for internal fault of sulfur hexafluoride electrical equipment | |
CN103017813B (en) | Comprehensive detection device of direct-current transmission valve cooling system instrument | |
CN104407122A (en) | Online parameter measurement system for transformer insulation oil | |
CN106969946B (en) | Condensed water sampling method and device for leak detection of condenser | |
CN109884263B (en) | Dissolved oxygen sensor test device and test method thereof | |
CN210136211U (en) | Quick analytical equipment of low temperature tank wagon dress product that fills | |
CN103590856A (en) | Monitoring method of mine gas beam tube line monitoring system | |
CN103615289A (en) | Mine gas bundle pipeline monitoring system | |
CN114397239A (en) | A device for online monitoring of microorganisms in fluid | |
CN219955068U (en) | Water flow detection device | |
CN208746789U (en) | A kind of two-compartment oil tank leak detecting device and system | |
CN203132798U (en) | Leakage monitoring device for direct inserting type condenser | |
CN105223297A (en) | The degasser that a kind of novel transformer oil chromatography on-Line Monitor Device is special | |
CN113847233B (en) | Water pump displacement testing system and method | |
CN209910899U (en) | Liquid immersion type leakage monitoring device for power equipment | |
CN209821181U (en) | Dissolved oxygen sensor test device | |
CN105259260A (en) | Novel transformer oil chromatography online monitoring device with three-way valve | |
CN112881867B (en) | Valve chamber insulation monitoring method | |
CN209230889U (en) | Platform with pipeline node leak detection | |
CN209542219U (en) | Sulfur hexafluoride leakage monitor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
AV01 | Patent right actively abandoned | ||
AV01 | Patent right actively abandoned | ||
AV01 | Patent right actively abandoned |
Granted publication date: 20171212 Effective date of abandoning: 20250328 |
|
AV01 | Patent right actively abandoned |
Granted publication date: 20171212 Effective date of abandoning: 20250328 |