WO2023240942A1 - 一种发电厂水汽模拟试验装置及方法 - Google Patents
一种发电厂水汽模拟试验装置及方法 Download PDFInfo
- Publication number
- WO2023240942A1 WO2023240942A1 PCT/CN2022/136151 CN2022136151W WO2023240942A1 WO 2023240942 A1 WO2023240942 A1 WO 2023240942A1 CN 2022136151 W CN2022136151 W CN 2022136151W WO 2023240942 A1 WO2023240942 A1 WO 2023240942A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water vapor
- pump
- online
- water
- desalted
- Prior art date
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 156
- 238000012360 testing method Methods 0.000 title claims abstract description 23
- 238000004088 simulation Methods 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title abstract description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 46
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000001301 oxygen Substances 0.000 claims abstract description 35
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 35
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 23
- 239000000126 substance Substances 0.000 claims abstract description 23
- 230000001105 regulatory effect Effects 0.000 claims abstract description 17
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 22
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 11
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 11
- 229910052742 iron Inorganic materials 0.000 claims description 11
- 229910052710 silicon Inorganic materials 0.000 claims description 11
- 239000010703 silicon Substances 0.000 claims description 11
- 229910052708 sodium Inorganic materials 0.000 claims description 11
- 239000011734 sodium Substances 0.000 claims description 11
- 239000005416 organic matter Substances 0.000 claims description 10
- 238000006392 deoxygenation reaction Methods 0.000 claims description 7
- 238000010998 test method Methods 0.000 claims description 4
- 238000009825 accumulation Methods 0.000 description 4
- 238000005260 corrosion Methods 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 230000009172 bursting Effects 0.000 description 3
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000010795 Steam Flooding Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Images
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/18—Water
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N17/00—Investigating resistance of materials to the weather, to corrosion, or to light
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0009—General constructional details of gas analysers, e.g. portable test equipment
- G01N33/0011—Sample conditioning
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0009—General constructional details of gas analysers, e.g. portable test equipment
- G01N33/0011—Sample conditioning
- G01N33/0016—Sample conditioning by regulating a physical variable, e.g. pressure, temperature
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0009—General constructional details of gas analysers, e.g. portable test equipment
- G01N33/0027—General constructional details of gas analysers, e.g. portable test equipment concerning the detector
- G01N33/0031—General constructional details of gas analysers, e.g. portable test equipment concerning the detector comprising two or more sensors, e.g. a sensor array
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0009—General constructional details of gas analysers, e.g. portable test equipment
- G01N33/0073—Control unit therefor
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Definitions
- This application belongs to the technical field of water vapor circulation system in power plants, and relates to a water vapor simulation test device and method in a power plant.
- Water vapor is an important working fluid for the operation of various thermal equipment in the water vapor circulation system of the power plant.
- the demineralized water in the boiler is heated by fuel to generate steam of a certain temperature and pressure.
- the steam drives the steam turbine to rotate at high speed, thereby driving the generator to generate electricity.
- the steam After completing the work, the steam It condenses into water and enters the water vapor circulation system again.
- the water vapor circulation system has extremely high requirements for the quality of water vapor, especially the conductivity, hydrogen conductivity, pH, Dissolved oxygen, sodium ions and other indicators.
- the purpose of this application is to overcome the shortcomings of the above-mentioned prior art and provide a water vapor simulation test device and method for a power plant.
- the system and method can accurately simulate water vapor in a power plant based on the characteristics and change patterns of water vapor components in the water vapor circulation system of the power plant. Test water samples are produced continuously.
- the power plant water vapor simulation test device described in this application includes a desalted water tank, a deoxygenation system, an ammonia adding pump, an oxygen adding pump, a water quality regulating pump, a thermostatic device, a flow meter, an online chemical instrument, and a simulated water vapor outlet.
- Valve and desalted water preparation system
- the desalted water tank is connected to the inlet of the deaerated system, and the outlet of the deoxygenated system is connected to the desalted water tank through a thermostatic device, a flow meter and a desalted water preparation system;
- the outlet of the ammonia adding pump, the outlet of the oxygen adding pump and the outlet of the water quality regulating pump are connected to the pipelines between the deaeration system and the constant temperature device;
- the online chemical instruments and simulated water vapor outlet valve are connected to the pipeline between the flow meter and the desalted water preparation system;
- the control system is connected with ammonia adding pump, oxygen adding pump, water quality regulating pump, thermostatic device and online chemical instrument.
- the online chemical instrument is one or a combination of online conductivity meter, online hydrogen conductivity, online pH meter, online sodium meter, online silicon meter, online iron meter and online organic matter analyzer.
- the desalted water tank is connected to the inlet of the deaeration system through the system pump.
- the pH is adjusted by an ammonia adding pump
- the oxygen content is adjusted by an oxygen adding pump
- one or a combination of hydrogen conductivity, sodium content, silicon content, iron content, and organic matter content is adjusted by a water quality regulating pump.
- the outlet of the deaeration system is connected to the desalted water tank through a return valve.
- the water vapor simulation test method for power plants described in this application includes the following steps:
- the desalted water in the desalted water tank enters the deaeration system for deoxygenation, and then goes through the ammonia adding pump to adjust the pH, the oxygen adding pump to adjust the oxygen content, and the water quality regulating pump to adjust the hydrogen conductivity, sodium content, silicon content, iron content, and organic matter.
- One or several combined components in the content are then constant-temperatured to a preset temperature by a thermostatic device, and then monitored by flow meters and online chemical instruments to simulate water vapor and water quality. Finally, they are divided into two channels, one of which is exposed to the outside world through the simulated water vapor outlet valve. output, and the other path is desalted by the desalted water preparation system and returned to the desalted water tank.
- the control system controls the dosage of ammonia adding pumps, oxygen adding pumps, and water quality regulating pumps based on the measured values of online chemical instruments. At the same time, it controls the thermostat device based on the set temperature value to prepare simulated water vapor of different temperatures and different components.
- the outlet of the deaeration system is connected to the desalted water tank through a return valve, and the flow of simulated water vapor is adjusted through the return valve.
- the desalted water in the desalted water tank is deoxygenated, pH adjusted, an oxygen pump is used to adjust the oxygen content, and a water quality adjusting pump is used to adjust the hydrogen conductivity and sodium content. , silicon content, iron content, organic matter content, one or more combinations of them, and then constant temperature to the preset temperature.
- the simulated water vapor parameters of the power plant are adjusted according to the measured values of the online chemical instruments, so as to Characteristics and changing patterns of water vapor components in the water vapor circulation system of power plants, accurately simulating water vapor in power plants, and continuously generating test water samples to study the impact and changes of water vapor quality in the water vapor circulation system on corrosion, salt accumulation, and pipe bursting of various thermal equipment for power plants.
- this application also realizes the recycling of water vapor in the system without any discharge of waste water or waste liquid, and has significant environmental benefits.
- Figure 1 is a schematic structural diagram of the present application.
- 1 is the desalted water tank
- 2 is the system pump
- 3 is the deaeration system
- 4 is the return valve
- 5 is the ammonia adding pump
- 6 is the oxygen adding pump
- 7 is the water quality regulating pump
- 8 is the thermostatic device
- 9 is the flow rate.
- 10 is the online chemical instrument
- 11 is the simulated water vapor outlet valve
- 12 is the desalted water preparation system
- 13 is the control system.
- the water vapor simulation test device of the power plant described in this application includes a desalted water tank 1, a system pump 2, a deaeration system 3, a return valve 4, an ammonia adding pump 5, an oxygen adding pump 6, a water quality regulating pump 7, a constant temperature Device 8, flow meter 9, online chemical instrument 10, simulated water vapor outlet valve 11 and desalted water preparation system 12;
- the desalted water tank 1 is connected to the inlet of the deaeration system 3 through the system pump 2.
- the outlet of the deaeration system 3 is divided into two paths. One path is connected to the desalted water tank 1 through the return valve 4, and the other path passes through the thermostatic device 8. , the flow meter 9 and the desalted water preparation system 12 are connected with the desalted water tank 1 .
- the outlet of the ammonia adding pump 5, the outlet of the oxygen adding pump 6 and the outlet of the water quality regulating pump 7 are connected with the pipelines between the deaeration system 3 and the thermostatic device 8.
- the pH is adjusted by the ammonia adding pump 5 and the oxygen adding pump 6.
- the oxygen content is adjusted by one or more combinations of hydrogen conductivity, sodium content, silicon content, iron content, and organic matter content through the water quality regulating pump 7 .
- the online chemical instrument 10 and the simulated water vapor outlet valve 11 are both connected to the pipeline between the flow meter 9 and the desalted water preparation system 12.
- the online chemical instrument 10 is an online conductivity meter, an online hydrogen conductivity meter, an online pH meter, and an online One or more of the sodium meter, online silicon meter, online iron meter and online organic matter analyzer are used to monitor the simulated water vapor water quality; the simulated water vapor is output to the outside through the simulated water vapor outlet valve 11 to provide continuous simulated water vapor for other tests.
- the control system 13 is connected to the ammonia adding pump 5, the oxygen adding pump 6, the water quality regulating pump 7, the thermostatic device 8 and the online chemical instrument 10, and controls the ammonia adding pump 5, the oxygen adding pump 6 and the water quality according to the measured values of the online chemical instrument 10 Adjust the dosage of pump 7; control the thermostat 8 according to the set temperature value to control the simulated water vapor under the set water quality conditions and temperature.
- the desalted water in the desalted water tank 1 enters the deaeration system 3 through the system pump 2 for deoxygenation, and desalination and deoxygenation water is obtained.
- the desalination and deoxygenation water is divided into two paths, of which one path flows back to the deaeration system through the return valve 4.
- the flow of water vapor is simulated by adjusting the opening of the return valve 4.
- the greater the opening of the return valve 4 the smaller the flow of simulated water vapor; the other channel sequentially adjusts the pH and the water vapor through the ammonia adding pump 5.
- the oxygen pump 6 adjusts the oxygen content and the water quality adjustment pump 7 adjusts one or more combinations of hydrogen conductivity, sodium content, silicon content, iron content, and organic matter content, and then the temperature is controlled to the preset temperature by the thermostatic device 8, and then The simulated water vapor water quality is monitored by the flow meter 9 and the online chemical instrument 10, and is finally divided into two paths. Among them, one path is output through the simulated water vapor outlet valve 11 to provide continuous simulated water vapor for other tests, and the other path is desalted through the desalted water preparation system 12 Then return to desalted water tank 1.
- the online chemical instrument 10 is one or more of an online conductivity meter, an online hydrogen conductivity meter, an online pH meter, an online sodium meter, an online silicon meter, an online iron meter, and an online organic matter analyzer.
- the control system 13 is based on the online
- the measurement value of the chemical instrument 10 controls the dosage of the ammonia adding pump 5, the oxygen adding pump 6, and the water quality regulating pump 7; the thermostatic device 8 is controlled according to the set temperature value, thereby preparing simulated water vapor with different temperatures and different components.
Abstract
一种发电厂水汽模拟试验装置及方法，试验装置中除盐水箱（1）与除氧系统（3）的入口相连通，除氧系统（3）的出口经过恒温装置（8）、流量计（9）及除盐水制备系统（12）与除盐水箱（1）相连通；加氨泵（5）的出口、加氧泵（6）的出口及水质调节泵（7）的出口与除氧系统（3）和恒温装置（8）之间的管道相连通；在线化学仪表（10）及模拟水汽出水阀（11）均与流量计（9）和除盐水制备系统（12）之间的管道相连通；控制系统（13）与加氨泵（5）、加氧泵（6）、水质调节泵（7）、恒温装置（8）及在线化学仪表（10）相连接，该系统及方法能够根据发电厂水汽循环系统水汽成分特质及变化规律，准确模拟发电厂水汽，连续产生试验水样。
Description
相关申请的交叉引用
本申请要求在2022年6月15日提交中国国家知识产权局、申请号为202210674811.4、发明名称为“一种发电厂水汽模拟试验装置及方法”的中国专利申请的优先权，其全部内容通过引用的方式并入本文中。
本申请属于发电厂水汽循环系统技术领域，涉及一种发电厂水汽模拟试验装置及方法。
水汽是发电厂水汽循环系统各热力设备运行的重要工质，通过燃料加热锅炉中的除盐水，产生一定温度和压力的蒸汽，蒸汽推动汽轮机高速旋转从而带动发电机发电，做完功后的蒸汽凝结为水从而再次进入水汽循环系统。在这一过程中，为了防止热力设备的腐蚀、积盐及爆管等各种事故的发生，水汽循环系统对水汽品质的要求极高，尤其是对水汽的电导率、氢电导率、pH、溶解氧、钠离子等指标。为了研究水汽循环系统水汽品质对各热力设备的腐蚀、积盐及爆管情况的影响及变化规律，因此需要针对发电厂水汽进行相关试验研究。因发电厂水汽主要成分为含有少量氨、一定量溶解氧和痕量级杂质离子的除盐水，很难人工模拟及制备，开展此类试验难度极大。
因此，如果能根据发电厂水汽循环系统水汽成分特质及变化规律，研究发明一种发电厂水汽模拟试验装置及方法，能够准确模拟发电厂水汽，连续产生试验水样，将彻底解决发电厂水汽相关试验研究难以开展的难题，为发电厂研究水汽循环系统水汽品质对各热力设备的腐蚀、积盐及爆管情况的影响及变化规律提供试验基础设施，对发电厂的安全经济运行有重要意义。
发明内容
本申请的目的在于克服上述现有技术的缺点，提供了一种发电厂水汽模拟试验装置及方法，该系统及方法能够根据发电厂水汽循环系统水汽成分特质及变化规律，准确模拟发电厂水汽，连续产生试验水样。
为达到上述目的，本申请所述的发电厂水汽模拟试验装置包括除盐水箱、除氧系统、加氨泵、加氧泵、水质调节泵、恒温装置、流量计、在线化学仪表、模拟水汽出水阀及除盐水制备系统；
除盐水箱与除氧系统的入口相连通，除氧系统的出口经过恒温装置、流量计及除盐水制备系统与除盐水箱相连通；
加氨泵的出口、加氧泵的出口及水质调节泵的出口与除氧系统和恒温装置之间的管道相连通；
在线化学仪表及模拟水汽出水阀均与流量计和除盐水制备系统之间的管道相连通；
控制系统与加氨泵、加氧泵、水质调节泵、恒温装置及在线化学仪表相连接。
在线化学仪表为在线电导率表、在线氢电导率、在线pH表、在线钠表、在线硅表、在线铁表及在线有机物分析仪中的一种或几种的组合。
除盐水箱经系统泵与除氧系统的入口相连通。
通过加氨泵调节pH，通过加氧泵调节氧含量，通过水质调节泵调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分。
除氧系统的出口经回流阀与除盐水箱相连通。
本申请所述的发电厂水汽模拟试验方法包括以下步骤：
除盐水箱中的除盐水进入除氧系统中进行除氧，再依次经过加氨泵调节pH、加氧泵调节氧含量及水质调节泵调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分，然后经恒温装置恒温至预设温度，再经流量计及在线化学仪表监测模拟水汽水质，最后分为两路，其中，一路通过模拟水汽出水阀对外输出，另一路经除盐水制备系统除盐后返回至除盐水箱。
控制系统根据在线化学仪表的测量值控制加氨泵、加氧泵、水质调节泵的加药量，同时根据设定温度值控制恒温装置，以制备出不同温度、不同成分的模拟水汽。
除氧系统的出口经回流阀与除盐水箱相连通，通过回流阀调节模拟水汽的流量。
本申请具有以下有益效果：
本申请所述的发电厂水汽模拟试验装置及方法在具体操作时，除盐水箱中的除盐水依次经除氧、调节pH、加氧泵调节氧含量及水质调节泵调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分，然后经恒温至预设温度，同时根据在线化学仪表的测量值，对模拟出的发电厂水汽参数进行调节，从而根据发电厂水汽循环系统水汽成分特质及变化规律，准确模拟发电厂水汽，连续产生试验水样，为发电厂研究水汽循环系统水汽品质对各热力设备的腐蚀、积盐及爆管情况的影响及变化规律提供试验基础设施。同时需要说明的是，本申请还实现了水汽在系统中循环利用，无任何废水、废液的排放，环保效益显著。
图1为本申请的结构示意图。
其中，1为除盐水箱、2为系统泵、3为除氧系统、4为回流阀、5为加氨泵、6为加氧泵、7为水质调节泵、8为恒温装置、9为流量计、10为在线化学仪表、11为模拟水汽出水阀、12为除盐水制备系统、13为控制系统。
为了使本技术领域的人员更好地理解本申请方案，下面将结合本申请实施例中的附图，对本申请实施例中的技术方案进行清楚、完整地描述，显然，所描述的实施例仅仅是本申请一部分的实施例，不是全部的实施例，而并非要限制本申请公开的范围。此外，在以下说明中，省略了对公知结构和技术的描述，以避免不必要的混淆本申请公开的概念。基于本申请中的实施例，本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例，都应当属于本申请保护的范围。
在附图中示出了根据本申请公开实施例的结构示意图。这些图并非是按比例绘制的，其中为了清楚表达的目的，放大了某些细节，并且可能省略了某些细节。图中所示出的各种区域、层的形状及它们之间的相对大小、位置 关系仅是示例性的，实际中可能由于制造公差或技术限制而有所偏差，并且本领域技术人员根据实际所需可以另外设计具有不同形状、大小、相对位置的区域/层。
参考图1，本申请所述的发电厂水汽模拟试验装置包括除盐水箱1、系统泵2、除氧系统3、回流阀4、加氨泵5、加氧泵6、水质调节泵7、恒温装置8、流量计9、在线化学仪表10、模拟水汽出水阀11及除盐水制备系统12；
除盐水箱1经系统泵2与除氧系统3的入口相连通，除氧系统3的出口分为两路，其中，一路经回流阀4与除盐水箱1相连通，另一路经过恒温装置8、流量计9及除盐水制备系统12与除盐水箱1相连通。
加氨泵5的出口、加氧泵6的出口及水质调节泵7的出口与除氧系统3和恒温装置8之间的管道相连通，通过加氨泵5调节pH，通过加氧泵6调节氧含量，通过水质调节泵7调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分。
在线化学仪表10及模拟水汽出水阀11均与流量计9和除盐水制备系统12之间的管道相连通，其中，在线化学仪表10为在线电导率表、在线氢电导率、在线pH表、在线钠表、在线硅表、在线铁表及在线有机物分析仪中的一种或几种，用于监测模拟水汽水质；通过模拟水汽出水阀11将模拟水汽对外输出，为其他试验提供连续模拟水汽。
控制系统13与加氨泵5、加氧泵6、水质调节泵7、恒温装置8及在线化学仪表10相连接，根据在线化学仪表10的测量值控制加氨泵5、加氧泵6及水质调节泵7的加药量；根据设定温度值控制恒温装置8，将模拟水汽控制在设定的水质条件及温度下。
本申请的具体工作过程为：
除盐水箱1中的除盐水经系统泵2进入除氧系统3中进行除氧，得除盐除氧水，所述除盐除氧水分为两路，其中，一路经回流阀4回流至除盐水箱1中，通过调节回流阀4的开度以模拟水汽的流量，其中，回流阀4的开度越大，则模拟水汽的流量越小；另一路依次经加氨泵5调节pH、加氧泵6调节氧含量及水质调节泵7调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分，然后经恒温装置8恒温至预设温度，再 经过流量计9及在线化学仪表10监测模拟水汽水质，最后分为两路，其中，一路通过模拟水汽出水阀11对外输出，为其他试验提供连续模拟水汽，另一路经除盐水制备系统12除盐后返回至除盐水箱1。
其中，在线化学仪表10为在线电导率表、在线氢电导率、在线pH表、在线钠表、在线硅表、在线铁表、在线有机物分析仪中的一种或几种，控制系统13根据在线化学仪表10的测量值控制加氨泵5、加氧泵6、水质调节泵7的加药量；根据设定温度值控制恒温装置8，从而制备出不同温度、不同成分的模拟水汽。
Claims (8)
- 一种发电厂水汽模拟试验装置，其特征在于，包括除盐水箱(1)、除氧系统(3)、加氨泵(5)、加氧泵(6)、水质调节泵(7)、恒温装置(8)、流量计(9)、在线化学仪表(10)、模拟水汽出水阀(11)及除盐水制备系统(12)；除盐水箱(1)与除氧系统(3)的入口相连通，除氧系统(3)的出口经过恒温装置(8)、流量计(9)及除盐水制备系统(12)与除盐水箱(1)相连通；加氨泵(5)的出口、加氧泵(6)的出口及水质调节泵(7)的出口与除氧系统(3)和恒温装置(8)之间的管道相连通；在线化学仪表(10)及模拟水汽出水阀(11)均与流量计(9)和除盐水制备系统(12)之间的管道相连通；控制系统(13)与加氨泵(5)、加氧泵(6)、水质调节泵(7)、恒温装置(8)及在线化学仪表(10)相连接。
- 根据权利要求1所述的发电厂水汽模拟试验装置，其特征在于，在线化学仪表(10)为在线电导率表、在线氢电导率、在线pH表、在线钠表、在线硅表、在线铁表及在线有机物分析仪中的一种或几种的组合。
- 根据权利要求1所述的发电厂水汽模拟试验装置，其特征在于，除盐水箱(1)经系统泵(2)与除氧系统(3)的入口相连通。
- 根据权利要求1所述的发电厂水汽模拟试验装置，其特征在于，通过加氨泵(5)调节pH，通过加氧泵(6)调节氧含量，通过水质调节泵(7)调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分。
- 根据权利要求1所述的发电厂水汽模拟试验装置，其特征在于，除氧系统(3)的出口经回流阀(4)与除盐水箱(1)相连通。
- 一种发电厂水汽模拟试验方法，其特征在于，包括以下步骤：除盐水箱(1)中的除盐水进入除氧系统(3)中进行除氧，再依次经过加氨 泵(5)调节pH、加氧泵(6)调节氧含量及水质调节泵(7)调节氢电导率、钠含量、硅含量、铁含量、有机物含量中的一种或几种的组合成分，然后经恒温装置(8)恒温至预设温度，再经流量计(9)及在线化学仪表(10)监测模拟水汽水质，最后分为两路，其中，一路通过模拟水汽出水阀(11)对外输出，另一路经除盐水制备系统(12)除盐后返回至除盐水箱(1)。
- 根据权利要求6所述的发电厂水汽模拟试验方法，其特征在于，控制系统(13)根据在线化学仪表(10)的测量值控制加氨泵(5)、加氧泵(6)、水质调节泵(7)的加药量，同时根据设定温度值控制恒温装置(8)，以制备出不同温度、不同成分的模拟水汽。
- 根据权利要求6所述的发电厂水汽模拟试验方法，其特征在于，除氧系统(3)的出口经回流阀(4)与除盐水箱(1)相连通，通过回流阀(4)调节模拟水汽的流量。
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210674811.4A CN115078670A (zh) | 2022-06-15 | 2022-06-15 | 一种发电厂水汽模拟试验装置及方法 |
| CN202210674811.4 | 2022-06-15 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2023240942A1 true WO2023240942A1 (zh) | 2023-12-21 |
Family
ID=83251398
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/CN2022/136151 WO2023240942A1 (zh) | 2022-06-15 | 2022-12-02 | 一种发电厂水汽模拟试验装置及方法 |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN115078670A (zh) |
| WO (1) | WO2023240942A1 (zh) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115078670A (zh) * | 2022-06-15 | 2022-09-20 | 西安热工研究院有限公司 | 一种发电厂水汽模拟试验装置及方法 |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090043406A1 (en) * | 2005-01-28 | 2009-02-12 | Abb Research Ltd. | System and Method for Planning the Operation of, Monitoring Processes in, Simulating, and Optimizing a Combined Power Generation and Water Desalination Plant |
| CN207263740U (zh) * | 2017-09-22 | 2018-04-20 | 中国大唐集团科学技术研究院有限公司华中分公司 | 火力发电厂热力系统水汽检测装置 |
| CN110294548A (zh) * | 2019-07-25 | 2019-10-01 | 西安热工研究院有限公司 | 一种凝结水精处理除盐系统运行模拟装置及方法 |
| CN112462700A (zh) * | 2020-11-09 | 2021-03-09 | 西安热工研究院有限公司 | 一种发电厂智慧化学水工况控制系统及方法 |
| CN213517098U (zh) * | 2020-09-30 | 2021-06-22 | 广东核电合营有限公司 | 电厂水质在线仪表评估试验装置 |
| CN215250020U (zh) * | 2021-03-19 | 2021-12-21 | 安徽华电宿州发电有限公司 | 一种智慧化学加药系统 |
| CN113848301A (zh) * | 2021-09-18 | 2021-12-28 | 西安热工研究院有限公司 | 一种火电厂高温高压蒸汽氧化在线实验系统及方法 |
| CN115078670A (zh) * | 2022-06-15 | 2022-09-20 | 西安热工研究院有限公司 | 一种发电厂水汽模拟试验装置及方法 |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108469355A (zh) * | 2018-06-08 | 2018-08-31 | 华能国际电力股份有限公司 | 一种发电厂汽水就地取样装置及取样方法 |
| CN111257375A (zh) * | 2020-03-23 | 2020-06-09 | 西安热工研究院有限公司 | 一种溶液电导率/溶液氢电导率的温度补偿系数试验装置及方法 |
| CN112129909B (zh) * | 2020-09-30 | 2024-03-12 | 广东核电合营有限公司 | 电厂水质在线仪表评估试验装置及试验方法 |
| CN113149266B (zh) * | 2021-03-19 | 2023-10-10 | 西安热工研究院有限公司 | 一种智慧化学加药系统及加药方法 |
-
2022
- 2022-06-15 CN CN202210674811.4A patent/CN115078670A/zh active Pending
- 2022-12-02 WO PCT/CN2022/136151 patent/WO2023240942A1/zh unknown
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090043406A1 (en) * | 2005-01-28 | 2009-02-12 | Abb Research Ltd. | System and Method for Planning the Operation of, Monitoring Processes in, Simulating, and Optimizing a Combined Power Generation and Water Desalination Plant |
| CN207263740U (zh) * | 2017-09-22 | 2018-04-20 | 中国大唐集团科学技术研究院有限公司华中分公司 | 火力发电厂热力系统水汽检测装置 |
| CN110294548A (zh) * | 2019-07-25 | 2019-10-01 | 西安热工研究院有限公司 | 一种凝结水精处理除盐系统运行模拟装置及方法 |
| CN213517098U (zh) * | 2020-09-30 | 2021-06-22 | 广东核电合营有限公司 | 电厂水质在线仪表评估试验装置 |
| CN112462700A (zh) * | 2020-11-09 | 2021-03-09 | 西安热工研究院有限公司 | 一种发电厂智慧化学水工况控制系统及方法 |
| CN215250020U (zh) * | 2021-03-19 | 2021-12-21 | 安徽华电宿州发电有限公司 | 一种智慧化学加药系统 |
| CN113848301A (zh) * | 2021-09-18 | 2021-12-28 | 西安热工研究院有限公司 | 一种火电厂高温高压蒸汽氧化在线实验系统及方法 |
| CN115078670A (zh) * | 2022-06-15 | 2022-09-20 | 西安热工研究院有限公司 | 一种发电厂水汽模拟试验装置及方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| CN115078670A (zh) | 2022-09-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2023240942A1 (zh) | 一种发电厂水汽模拟试验装置及方法 | |
| CN103207210B (zh) | 一种湿蒸汽干度在线测量仪 | |
| CN109078931A (zh) | 高温气冷堆核电机组二回路化学清洗的动态模拟试验装置及使用方法 | |
| CN201273899Y (zh) | 一种循环水阻垢剂评价试验装置 | |
| CN111551482B (zh) | 高温高压一、二回路联动运行的综合动水腐蚀试验装置 | |
| CN101642071A (zh) | 水体总溶解气体过饱和生成及其对鱼类影响研究的装置 | |
| CN105223128A (zh) | 电化学测量方式的电站流动加速腐蚀模拟实验管路装置 | |
| CN108469390B (zh) | 可拆卸环道式单相流冲蚀试验装置 | |
| WO2022193562A1 (zh) | 一种在线化学仪表智慧校验维护系统及方法 | |
| CN107907301B (zh) | 一种高温高压水气流体效应模拟装置 | |
| CN105719708A (zh) | 基于反应堆第4级降压系统t型管夹带试验系统及方法 | |
| Zhang et al. | Experimental study on the transverse mixing of 5× 5 helical cruciform fuel assembly by wire mesh sensor | |
| CN110783006B (zh) | 一种除气试验装置及方法 | |
| CN106092351B (zh) | 核电站管道内壁温度测量方法和装置 | |
| CN201479739U (zh) | 水体总溶解气体过饱和生成及其对鱼类影响研究的装置 | |
| CN112394023A (zh) | 一种核岛设备冷却水系统材料腐蚀模拟装置及其使用方法 | |
| JP5519920B2 (ja) | Ｐｗｒ発電所二次冷却系の水処理システム及びその方法 | |
| CN112881639A (zh) | 一种现场就地在线化学仪表智能检验校准系统 | |
| CN102706397A (zh) | 大管径低压头水流量测量装置及方法 | |
| CN110473639B (zh) | 一种用于研究粉尘沉积行为的装置 | |
| CN203811572U (zh) | 发电机铜线棒腐蚀速率电化学在线监测系统 | |
| CN116818997A (zh) | 一种阻垢剂性能测试装置及方法 | |
| CN212622559U (zh) | 一种发电厂水汽系统腐蚀控制装置 | |
| CN111540492B (zh) | 一、二回路联动运行的综合动水腐蚀试验装置及方法 | |
| KR101386698B1 (ko) | 부식 산화막 생성 시스템, 및 이를 이용한 모사된 원자로 1차 계통의 부식시험방법 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 22946608 Country of ref document: EP Kind code of ref document: A1 |