CN204834063U - Active waste heat discharge heat exchanger test device of non - - Google Patents
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- CN204834063U CN204834063U CN201520454527.1U CN201520454527U CN204834063U CN 204834063 U CN204834063 U CN 204834063U CN 201520454527 U CN201520454527 U CN 201520454527U CN 204834063 U CN204834063 U CN 204834063U
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- 238000012360 testing method Methods 0.000 title claims abstract description 110
- 239000002918 waste heat Substances 0.000 title claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 135
- 238000012546 transfer Methods 0.000 claims abstract description 125
- 239000003381 stabilizer Substances 0.000 claims abstract description 19
- 238000000034 method Methods 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 10
- 239000007921 spray Substances 0.000 claims abstract description 10
- 239000000498 cooling water Substances 0.000 claims description 59
- 239000012530 fluid Substances 0.000 claims description 19
- 239000010963 304 stainless steel Substances 0.000 claims description 16
- 229910000589 SAE 304 stainless steel Inorganic materials 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 230000006641 stabilisation Effects 0.000 claims description 3
- 238000011105 stabilization Methods 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 238000013461 design Methods 0.000 abstract description 7
- 230000005514 two-phase flow Effects 0.000 description 7
- 238000001816 cooling Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 229910001098 inconels 690 Inorganic materials 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910001055 inconels 600 Inorganic materials 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 229910001026 inconel Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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- 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
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- 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
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Abstract
本实用新型涉及一种非能动余热排出热交换器试验装置。所述试验装置包括传热试验段、稳压器、屏蔽泵、加热器、循环泵、换热器、高位水箱、低位水箱、提升泵、补水泵和喷淋泵;其中,所述传热试验段、稳压器、屏蔽泵、加热器组成试验装置的主回路系统;所述传热试验段包括3根C形传热管和冷却水箱,所述稳压器与传热试验段的出口管道和屏蔽泵的入口管道相连;所述屏蔽泵与传热试验段的出口管道相连,通过调节屏蔽泵前的阀门和旁通阀门,调节主回路的流量;所述加热器安装在屏蔽泵和传热试验段之间。本实用新型对传热管的形式、尺寸、材质的设计合理。且合理避免了应力变形问题,同时也大大减少了用水量。能够更准确地模拟传热过程,获取更精确的传热数据。
The utility model relates to a test device for a passive waste heat discharge heat exchanger. The test device includes a heat transfer test section, a voltage stabilizer, a shielded pump, a heater, a circulating pump, a heat exchanger, a high-level water tank, a low-level water tank, a lift pump, a water supply pump and a spray pump; wherein, the heat transfer test section, a voltage stabilizer, a shielded pump, and a heater form the main circuit system of the test device; It is connected with the inlet pipe of the shielded pump; the shielded pump is connected with the outlet pipe of the heat transfer test section, and the flow of the main circuit is adjusted by adjusting the valve and bypass valve in front of the shielded pump; the heater is installed between the shielded pump and the heat transfer test section. between heat test sections. The utility model has reasonable designs on the form, size and material of the heat transfer tube. And the problem of stress deformation is reasonably avoided, and the water consumption is also greatly reduced. The heat transfer process can be simulated more accurately and more accurate heat transfer data can be obtained.
Description
技术领域technical field
本发明具体涉及一种非能动余热排出热交换器试验装置。The invention specifically relates to a test device for a passive waste heat discharge heat exchanger.
背景技术Background technique
非能动余热排出热交换器(PRHRHX)是第三代压水堆核电站AP1000中的应急堆芯冷却系统,对缓解热阱丧失事故起着重要作用。非能动余热排出热交换器主要由传热管和安全壳内换料水箱组成。反应堆冷却剂系统热段的流体流入传热管,被换料水箱中的水冷却,从而将堆芯的衰变热排出。由于不同温度的冷却剂之间存在密度差,在热交换器中形成了自然循环。Passive waste heat removal heat exchanger (PRHRHX) is an emergency core cooling system in AP1000 of the third-generation pressurized water reactor nuclear power plant, which plays an important role in alleviating heat sink loss accidents. The passive waste heat removal heat exchanger is mainly composed of heat transfer tubes and refueling water tanks in the containment. The fluid in the hot section of the reactor coolant system flows into the heat transfer tubes and is cooled by the water in the refueling water tank, thereby removing the decay heat of the core. Due to the density difference between the coolants of different temperatures, a natural circulation is formed in the heat exchanger.
非能动余热排出热交换器在自然循环过程中的两相流动传热现象是对反应堆安全有重要影响的热工水力现象。由于热交换器一、二次侧温差大,参数变化范围广,涉及多种单相和两相流动传热模式。自然循环流速低,受浮升力影响大,因此热交换器中的动力学特性与强迫循环有显著不同。目前,对非能动余热排出热交换器传热管内、外的两相流动及传热现象认识不充分,因此,建立非能动余热排出热交换器试验装置用于开展自然循环两相流动传热行为研究对于堆芯设计和安全分析技术的发展十分必要。The two-phase flow heat transfer phenomenon of the passive waste heat removal heat exchanger in the natural circulation process is a thermal-hydraulic phenomenon that has an important impact on the safety of the reactor. Due to the large temperature difference between the primary and secondary sides of the heat exchanger, the parameters vary widely, involving a variety of single-phase and two-phase flow heat transfer modes. Natural circulation has a low flow rate and is greatly affected by buoyancy, so the dynamics in the heat exchanger are significantly different from forced circulation. At present, there is insufficient understanding of the two-phase flow and heat transfer phenomenon inside and outside the heat transfer tube of the passive waste heat removal heat exchanger. Therefore, the experimental device of the passive waste heat removal heat exchanger is established to carry out the heat transfer behavior of the natural circulation two-phase flow Research is necessary for the development of core design and safety analysis techniques.
美国西屋公司针对AP600中的非能动余热排出热交换器建立了传热试验装置,用于验证热交换器的传热性能。试验装置的试验段由3根并排的304不锈钢竖直传热管浸没在圆形水箱中,模拟热交换器换热管的竖直段在换料水箱中的传热。装置保持了AP600非能动余热排出热交换器的完全高度,换热管的壁厚、内径及间距与真实尺寸相似。试验装置的运行工况能够涵盖AP600非能动余热排出热交换器的运行参数。但是,实际AP1000的热交换器传热管是C形传热管,由上、下水平段和竖直段组成,其中水平段占传热管总表面积的42%,主要的传热发生在传热管上水平段。而在西屋公司建立的试验装置中,传热管只包含竖直段,在该装置上不能开展水平段的传热试验研究。同时,该试验装置的传热管采用304不锈钢管,而AP1000中的传热管材质为因科镍(Inconel690),两种材质的热导率相差约34%,这将对传热试验数据的准确性和可靠性产生影响。Westinghouse Corporation of the United States has established a heat transfer test device for the passive waste heat removal heat exchanger in AP600 to verify the heat transfer performance of the heat exchanger. The test section of the test device consisted of three parallel 304 stainless steel vertical heat transfer tubes immersed in a circular water tank to simulate the heat transfer of the vertical section of the heat exchanger tube in the refueling water tank. The device maintains the full height of the AP600 passive waste heat removal heat exchanger, and the wall thickness, inner diameter and spacing of the heat exchange tubes are similar to the real size. The operating conditions of the test device can cover the operating parameters of the AP600 passive waste heat removal heat exchanger. However, the heat transfer tube of the actual AP1000 heat exchanger is a C-shaped heat transfer tube, which is composed of upper and lower horizontal sections and vertical sections, of which the horizontal section accounts for 42% of the total surface area of the heat transfer tube, and the main heat transfer occurs in the The upper horizontal section of the heat pipe. In the test device established by Westinghouse, the heat transfer tube only includes the vertical section, and the heat transfer test research of the horizontal section cannot be carried out on this device. At the same time, the heat transfer tube of the test device is made of 304 stainless steel tube, while the material of the heat transfer tube in AP1000 is Inconel (Inconel690). Accuracy and reliability have an impact.
发明内容Contents of the invention
针对上述试验装置的不足,本发明的目的在于建立与AP1000非能动余热排出热交换器C形管尺寸相同、材质接近的非能动余热排出热交换器传热试验装置,用于开展自然循环两相流动传热试验,为堆芯设计和安全分析提供试验数据,并为非能动余热排出热交换器自然循环两相流动传热程序模型的评价提供依据。In view of the deficiencies of the above-mentioned test device, the purpose of the present invention is to establish a passive waste heat discharge heat exchanger heat transfer test device with the same size and similar material as the C-shaped tube of the AP1000 passive waste heat discharge heat exchanger, which is used to carry out natural circulation two-phase The flow heat transfer test provides test data for core design and safety analysis, and provides a basis for the evaluation of the passive waste heat removal heat exchanger natural circulation two-phase flow heat transfer program model.
为达到以上目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种非能动余热排出热交换器试验装置,所述试验装置包括传热试验段、稳压器、屏蔽泵、加热器、循环泵、换热器、高位水箱、低位水箱、提升泵、补水泵和喷淋泵;A passive waste heat discharge heat exchanger test device, the test device includes a heat transfer test section, a voltage stabilizer, a shielded pump, a heater, a circulation pump, a heat exchanger, a high-level water tank, a low-level water tank, a lift pump, and a water supply pump and spray pumps;
其中,所述传热试验段、稳压器、屏蔽泵、加热器组成试验装置的主回路系统;所述传热试验段包括3根C形传热管和冷却水箱,所述稳压器与传热试验段的出口管道和屏蔽泵的入口管道相连;所述屏蔽泵与传热试验段的出口管道相连,通过调节屏蔽泵前的阀门和旁通阀门,调节主回路的流量;所述加热器安装在屏蔽泵和传热试验段之间;Wherein, the heat transfer test section, voltage stabilizer, shielded pump, and heater form the main circuit system of the test device; the heat transfer test section includes 3 C-shaped heat transfer tubes and a cooling water tank, and the voltage stabilizer and The outlet pipe of the heat transfer test section is connected to the inlet pipe of the shielded pump; the shielded pump is connected to the outlet pipe of the heat transfer test section, and the flow of the main circuit is adjusted by adjusting the valve and the bypass valve in front of the shielded pump; the heating The device is installed between the shielded pump and the heat transfer test section;
所述循环泵的入口与换热器的管程出口连接,出口与冷却水箱的入口管相连;The inlet of the circulating pump is connected to the tube-side outlet of the heat exchanger, and the outlet is connected to the inlet pipe of the cooling water tank;
所述换热器的管程入口与冷却水箱的出口管相连,管程出口与循环泵的入口相连;The tube-side inlet of the heat exchanger is connected to the outlet pipe of the cooling water tank, and the tube-side outlet is connected to the inlet of the circulation pump;
所述高位水箱储存主回路系统用纯水,在重力作用下向主回路系统注水;低位水箱储存主回路系统用纯水;The high-level water tank stores pure water for the main circuit system, and injects water into the main circuit system under the action of gravity; the low-level water tank stores pure water for the main circuit system;
所述提升泵与高位水箱和低位水箱相连,将低位水箱中的水注入高位水箱中;补水泵安装在低位水箱和稳压器下管口之间,将低位水箱中的水从稳压器底部注入,提升稳压器压力,且保证稳压器内的水面不低于最低液位值;喷淋泵安装在低位水箱和稳压器上管口之间,将低位水箱中的水通过稳压器顶部喷淋装置向稳压器中注水。The lifting pump is connected with the high-level water tank and the low-level water tank, and injects the water in the low-level water tank into the high-level water tank; Inject, increase the pressure of the regulator, and ensure that the water level in the regulator is not lower than the minimum liquid level value; the spray pump is installed between the low-level water tank and the upper nozzle of the regulator, and the water in the low-level water tank passes through the stabilized pressure The sprinkler at the top of the regulator injects water into the regulator.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述传热试验段中,每根C形管12由上水平段、竖直段和下水平段三段用卡套连接而成,3根传热管是分别嵌套在冷却水箱的3个竖直圆管中;3根传热管的入口和出口分别通过上分流器、下分流器与试验装置主回路管道相连。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, in the heat transfer test section, each C-shaped pipe 12 is connected by ferrules in three sections: the upper horizontal section, the vertical section and the lower horizontal section. The three heat transfer tubes are respectively nested in the three vertical circular tubes of the cooling water tank; the inlet and outlet of the three heat transfer tubes are respectively connected to the main circuit pipe of the test device through the upper splitter and the lower splitter.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述冷却水箱由3个竖直圆管并联与上、下水平圆管连接而成,每个竖直圆管中分别包含了一根传热管的竖直段;冷却水箱底部的下水平圆管上具有入口管,上水平圆管具有上法兰盖,所述上法兰盖上具有出口管,上法兰盖上还有另一个出口管用于冷却水的溢流。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the cooling water tank is formed by connecting three vertical circular tubes in parallel with the upper and lower horizontal circular tubes, and each vertical circular tube contains The vertical section of a heat transfer tube; the lower horizontal circular tube at the bottom of the cooling water tank has an inlet pipe, the upper horizontal circular tube has an upper flange cover, and the upper flange cover has an outlet pipe, and the upper flange cover also has an outlet pipe. There is another outlet pipe for overflow of cooling water.
进一步地,如上所述的非能动余热排出热交换器试验装置,在所述传热管中布置数根热偶阱,热偶阱插入传热管中并与传热管壁面银焊,用三脚支架将其支撑在传热管中心,热电偶从热偶阱的开口端穿进去,在3根传热管中分别布置10根、12根和13根热电偶;3根传热管外壁面具有直接焊接在外壁面的热电偶,上述3根传热管外壁面分别布置10根、14根和13根热电偶,上述外壁面的热电偶与传热管中的热电偶交错分布;在所述冷却水箱中布置18根热偶阱,热偶阱插入冷却水箱中,并与水箱壁面焊接,热电偶穿进热偶阱中,每个热偶阱中安装1根热电偶。Further, in the above-mentioned passive waste heat removal heat exchanger test device, several thermocouple traps are arranged in the heat transfer tube, and the thermocouple traps are inserted into the heat transfer tube and silver-welded with the wall surface of the heat transfer tube. The bracket supports it in the center of the heat transfer tube, and the thermocouples penetrate through the opening end of the thermocouple well, and 10, 12 and 13 thermocouples are respectively arranged in the 3 heat transfer tubes; the outer walls of the 3 heat transfer tubes have The thermocouples directly welded on the outer wall surface, 10, 14 and 13 thermocouples are respectively arranged on the outer walls of the above three heat transfer tubes, and the thermocouples on the outer wall surface and the thermocouples in the heat transfer tubes are distributed alternately; 18 thermocouple wells are arranged in the water tank. The thermocouple wells are inserted into the cooling water tank and welded to the wall of the water tank. The thermocouples penetrate into the thermocouple wells, and one thermocouple is installed in each thermocouple well.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述稳压器采用立式圆柱形结构,并且有上、下椭圆形封头,稳压器稳压过程中,容器内气体排放由排气阀实现,排气阀安装在稳压器的顶端;系统压力保护通过安装在稳压器上端的安全阀实现。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the pressurizer adopts a vertical cylindrical structure and has upper and lower elliptical heads. During the pressure stabilization process of the pressurizer, the gas in the container The discharge is realized by the exhaust valve, which is installed on the top of the voltage stabilizer; the system pressure protection is realized by the safety valve installed on the upper end of the voltage stabilizer.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述加热器与主回路管道通过法兰连接,法兰间加绝缘密封垫片;主回路流体流经加热器,再经上分流器流入传热管;加热器最大工作压力为15MPa,最大工作温度为324℃;加热器内工质为纯水,加热器采用Φ32×3mm、长度约4.5m的管子制成,加热器采用经可控硅整流电源整定后的直流低电压大电流直接输出到加热管段上的加热方式,整流电源输出为12脉波直流DC:50V、0~10000A,加热电功率为300KW,管道中间接电源正极,两端接电源负极。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the heater is connected to the main circuit pipeline through flanges, and insulating sealing gaskets are added between the flanges; the main circuit fluid flows through the heater, and then passes through the upper The shunt flows into the heat transfer tube; the maximum working pressure of the heater is 15MPa, and the maximum working temperature is 324°C; the working medium in the heater is pure water, and the heater is made of a pipe with a diameter of 32×3mm and a length of about 4.5m. The DC low voltage and high current adjusted by the thyristor rectifier power supply is directly output to the heating pipe section for heating. The output of the rectifier power supply is 12-pulse DC DC: 50V, 0-10000A, the heating power is 300KW, and the positive pole of the indirect power supply in the pipeline , both ends are connected to the negative pole of the power supply.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述循环泵将冷却水箱内的水抽出,经换热器冷却后,再注入冷却水箱,实现冷却水箱内水的循环和温度恒定。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the circulation pump pumps out the water in the cooling water tank, and after being cooled by the heat exchanger, injects it into the cooling water tank to realize the circulation and temperature of the water in the cooling water tank. constant.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述换热器降低从冷却水箱出来的流体温度,以实现冷却水箱内水温恒定,换热器为蒸发式换热器,采用管壳式结构,立式布置,管程换热管采用U型布置,壳程为圆柱筒体结构,筒体与上下封头连接,上封头为椭圆形封头,下封头为球形封头,壳程和管程材质均为304不锈钢。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the heat exchanger lowers the temperature of the fluid coming out of the cooling water tank to achieve a constant water temperature in the cooling water tank, and the heat exchanger is an evaporative heat exchanger. Shell-and-tube structure, vertical arrangement, tube side heat exchange tube adopts U-shaped arrangement, shell side is a cylindrical structure, the cylinder is connected with the upper and lower heads, the upper head is an elliptical head, and the lower head is a spherical head. Head, shell side and tube side are made of 304 stainless steel.
进一步地,如上所述的非能动余热排出热交换器试验装置,所述热偶阱使用Φ3×0.5mm的304不锈钢无缝管制作而成,钢管一端封闭,一端开口。Furthermore, in the above-mentioned passive waste heat removal heat exchanger test device, the thermocouple trap is made of Φ3×0.5mm 304 stainless steel seamless pipe, one end of the steel pipe is closed and the other end is open.
进一步地,如上所述的非能动余热排出热交换器试验装置,高位水箱为直径1m、高1.2m的圆柱形水箱,水箱工作温度为20~90℃,工作压力为常压,水箱材质为304不锈钢;低位水箱为1×1×1.3m的立方体水箱,水箱工作温度为20~90℃,工作压力为常压,水箱材质为304不锈钢。Further, in the above-mentioned passive waste heat discharge heat exchanger test device, the high-level water tank is a cylindrical water tank with a diameter of 1m and a height of 1.2m. The working temperature of the water tank is 20-90℃, the working pressure is normal pressure, and the material of the water tank is 304 Stainless steel; the lower water tank is a cubic water tank of 1×1×1.3m, the working temperature of the water tank is 20-90°C, the working pressure is normal pressure, and the material of the water tank is 304 stainless steel.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
本发明的非能动余热排出热交换器试验装置采用了3根Φ19.05×1.5mm的Inconel600C形管模拟AP1000中热交换器的传热管,其尺寸与AP1000中的三根典型传热管相同。相比较304不锈钢材质,Inconel600的热导率与Inconel690更为接近,仅相差6%。The passive waste heat discharge heat exchanger test device of the present invention uses three Φ19.05×1.5mm Inconel600C-shaped tubes to simulate the heat transfer tubes of the heat exchanger in AP1000, and its size is the same as the three typical heat transfer tubes in AP1000. Compared with 304 stainless steel, the thermal conductivity of Inconel600 is closer to that of Inconel690, with a difference of only 6%.
此外,对冷却水箱采取的简化设计,合理避免了由于水箱尺寸过大引起的应力变形问题,同时也大大减少了冷却水箱的用水量,缩短了试验准备时间。In addition, the simplified design of the cooling water tank reasonably avoids the stress deformation problem caused by the oversized water tank, and also greatly reduces the water consumption of the cooling water tank and shortens the test preparation time.
经过调试,该试验装置能达到压力0.2~15.0MPa、传热管入口含汽率-0.1~1.0、入口温度150~324℃、传热管内流率200~2000kg/m2s的试验工况范围。该工况范围涵盖了AP1000非能动余热排出热交换器的工作范围。After debugging, the test device can reach the test range of pressure 0.2-15.0MPa, heat transfer tube inlet vapor content -0.1-1.0, inlet temperature 150-324°C, heat transfer tube internal flow rate 200-2000kg/m 2 s . This operating range covers the operating range of the AP1000 passive waste heat removal heat exchanger.
因此,在该装置上开展自然循环两相流动传热试验能够更准确地模拟AP1000非能动余热排出热交换器的传热过程,获取更精确的传热数据。Therefore, carrying out the natural circulation two-phase flow heat transfer test on this device can more accurately simulate the heat transfer process of the AP1000 passive waste heat removal heat exchanger and obtain more accurate heat transfer data.
附图说明Description of drawings
图1为非能动余热排出热交换器实验装置流程图。Figure 1 is a flow chart of the experimental device for passive waste heat removal heat exchanger.
图2为传热试验段结构示意图。Figure 2 is a schematic diagram of the structure of the heat transfer test section.
图3为热偶阱结构示意图。Figure 3 is a schematic diagram of the structure of a thermocouple well.
具体实施方式Detailed ways
下面结合附图和实施例对本发明进行详细的描述。The present invention will be described in detail below in conjunction with the accompanying drawings and embodiments.
如图1所示,非能动余热排出热交换器试验装置包括传热试验段1、稳压器2、屏蔽泵3、加热器4、循环泵5、换热器6、高位水箱7、低位水箱8、提升泵9、补水泵10和喷淋泵11。其中,试验段1、稳压器2、屏蔽泵3、加热器4组成了试验装置的主回路系统。As shown in Figure 1, the passive waste heat removal heat exchanger test device includes a heat transfer test section 1, a voltage stabilizer 2, a shielded pump 3, a heater 4, a circulation pump 5, a heat exchanger 6, a high-level water tank 7, and a low-level water tank 8. Lifting pump 9, replenishment pump 10 and spray pump 11. Among them, the test section 1, the voltage stabilizer 2, the shielded pump 3, and the heater 4 constitute the main circuit system of the test device.
流体在主回路中流经加热器4时,温度上升,密度下降,于是向上流动进入传热试验段1。在传热试验段1中,主回路流体被冷却,密度增大,于是向下流动,流出试验段,再经主回路管道回到加热器4。这就在非能动余热排出热交换器试验装置中形成了自然循环过程。如果开启阀门VAJ101和VAJ102,并开启屏蔽泵3,主回路流体经过屏蔽泵再进入加热器,这就形成了强迫循环。When the fluid flows through the heater 4 in the main circuit, the temperature rises and the density drops, so it flows upwards into the heat transfer test section 1 . In the heat transfer test section 1, the main circuit fluid is cooled and its density increases, so it flows downward, flows out of the test section, and returns to the heater 4 through the main circuit pipe. This forms a natural circulation process in the passive waste heat removal heat exchanger test device. If the valves VAJ101 and VAJ102 are opened, and the canned pump 3 is turned on, the main circuit fluid passes through the canned pump and then enters the heater, which forms a forced circulation.
(1)传热试验段(1) Heat transfer test section
传热试验段1是试验装置中的关键部件,用于将主回路中的热量传递到二次侧系统。如图2所示,其主要由3根C形传热管12和冷却水箱13组成。C形管12浸没在冷却水箱13中,冷却水箱13模拟的是安全壳内换料水箱。Heat transfer test section 1 is a key component in the test device, which is used to transfer the heat in the primary circuit to the secondary side system. As shown in FIG. 2 , it mainly consists of three C-shaped heat transfer tubes 12 and a cooling water tank 13 . The C-shaped pipe 12 is submerged in the cooling water tank 13, which simulates the refueling water tank in the containment.
试验段1的主要技术参数如表1所示。The main technical parameters of test section 1 are shown in Table 1.
表1传热试验段主要技术参数Table 1 Main technical parameters of heat transfer test section
传热管12的尺寸与AP1000中的传热管尺寸相同,外径为19.05mm,壁厚1.65mm。每根C形管12由上水平段、竖直段和下水平段三段用卡套连接而成。采用卡套连接而不使用整根C形管,是出于方便试验段安装的考虑。因为3根传热管12是分别嵌套在冷却水箱13的3个竖直圆管中的。The size of the heat transfer tube 12 is the same as that of the AP1000, with an outer diameter of 19.05 mm and a wall thickness of 1.65 mm. Every C-shaped pipe 12 is formed by connecting three sections of the upper horizontal section, the vertical section and the lower horizontal section with ferrules. The use of the ferrule connection instead of the entire C-shaped pipe is for the convenience of the installation of the test section. Because the three heat transfer tubes 12 are respectively nested in the three vertical circular tubes of the cooling water tank 13 .
3根传热管12分别模拟了AP1000非能动余热排出热交换器传热管束中的最短、最长和中心处的传热管(如表2所示)。传热管束在同一竖直平面内,相邻水平段中心轴间距设计为38mm,与AP1000相同。传热管12的材质为Inconel600,其热导率与Inconel690仅相差6%。The three heat transfer tubes 12 respectively simulate the shortest, longest and central heat transfer tubes in the heat transfer tube bundle of the AP1000 passive waste heat removal heat exchanger (as shown in Table 2). The heat transfer tube bundles are in the same vertical plane, and the distance between the central axes of adjacent horizontal sections is designed to be 38mm, which is the same as AP1000. The material of the heat transfer tube 12 is Inconel600, and its thermal conductivity is only 6% different from that of Inconel690.
表2传热管长度Table 2 Heat Transfer Tube Length
3根传热管12的入口和出口分别通过上分流器14、下分流器15与试验装置主回路管道相连。流体从上分流器14流入传热管12,从下分流器15流出传热管12。当高温流体流经传热管时12,冷却水箱13中的水被加热甚至沸腾,主回路中的热量就通过热交换器传热管束传至冷却水箱13。出口管线冷水与入口管线热水之间的密度差使得流体在主回路中形成了自然循环。The inlets and outlets of the three heat transfer tubes 12 are respectively connected to the main loop pipe of the test device through the upper splitter 14 and the lower splitter 15 . The fluid flows into the heat transfer tube 12 from the upper splitter 14 and flows out of the heat transfer tube 12 from the lower splitter 15 . When the high-temperature fluid flows through the heat transfer tubes 12, the water in the cooling water tank 13 is heated or even boiled, and the heat in the main circuit is transferred to the cooling water tank 13 through the heat transfer tube bundle of the heat exchanger. The difference in density between the cold water in the outlet line and the hot water in the inlet line creates a natural circulation of the fluid in the primary circuit.
冷却水箱13由3个竖直圆管并联与上下水平圆管连接而成。每个竖直圆管中分别包含了一根传热管12的竖直段。水平圆管尺寸为Φ325×3.5mm,竖直圆管尺寸为Φ219×3.5mm。根据西屋公司对AP600非能动余热排出热交换器的试验研究表明,相邻传热管轴间距较大时,管束之间的热效应相互独立。典型的热交换器传热管管间距与直径比P/D为1.3-1.5,AP600中P/D=2。当冷却水箱壁面与传热管的距离足够大时,水箱壁面的距离变化对传热管内外传热的影响可以忽略。本装置中,冷却水箱13壁面与传热管12距离大于38mm,不会影响主回路与冷却水的传热,因此对冷却水箱的合理简化是可行的。The cooling water tank 13 is formed by connecting three vertical round pipes in parallel with the upper and lower horizontal round pipes. Each vertical circular tube contains a vertical section of the heat transfer tube 12 respectively. The size of the horizontal round tube is Φ325×3.5mm, and the size of the vertical round tube is Φ219×3.5mm. According to Westinghouse's experimental research on the AP600 passive waste heat removal heat exchanger, it is shown that when the axial distance between adjacent heat transfer tubes is large, the thermal effects between the tube bundles are independent of each other. Typical heat exchanger tube spacing and diameter ratio P/D is 1.3-1.5, and P/D=2 in AP600. When the distance between the wall of the cooling water tank and the heat transfer tube is large enough, the influence of the distance change of the wall of the water tank on the heat transfer inside and outside the heat transfer tube can be ignored. In this device, the distance between the wall of the cooling water tank 13 and the heat transfer tube 12 is greater than 38mm, which will not affect the heat transfer between the main circuit and the cooling water, so it is feasible to reasonably simplify the cooling water tank.
冷却水箱13的主要技术参数如表3所示。二次侧的冷却水从冷却水箱13底部的入口管16流进去,从上法兰盖17上的出口管18流出。上法兰盖上还有另一个出口管19用于冷却水的溢流。The main technical parameters of the cooling water tank 13 are shown in Table 3. The cooling water on the secondary side flows in from the inlet pipe 16 at the bottom of the cooling water tank 13 and flows out from the outlet pipe 18 on the upper flange cover 17 . There is also another outlet pipe 19 on the upper flange cover for the overflow of cooling water.
表3冷却水箱主要技术参数Table 3 Main technical parameters of cooling water tank
为了获取自然循环两相流动传热试验数据,试验段1中布置了许多温度测点,包括传热管12中心流体温度、外壁面温度和冷却水箱13池水温度。In order to obtain the test data of natural circulation two-phase flow heat transfer, many temperature measuring points were arranged in the test section 1, including the temperature of the fluid in the center of the heat transfer tube 12, the temperature of the outer wall, and the temperature of the pool water in the cooling water tank 13.
如图3所示,为测量传热管12中心流体温度,在传热管12中布置了数根热偶阱20。热偶阱插入传热管12中并与传热管12壁面银焊,用三脚支架21将其支撑在传热管12中心。直径为0.5mm的铠装热电偶从热偶阱20的开口端穿进去。根据试验数据需要,本试验装置需要在A传热管12中布置10根热电偶,在B传热管12中布置12根热电偶,在C传热管12中布置13根热电偶。热偶阱尺寸的选取既要保证能够穿入足够数量的热电偶,又要尽可能减小其对传热管内流体流动的影响,同时,还要满足20MPa、350℃的设计条件。因此,热偶阱20使用Φ3×0.5mm的304不锈钢无缝管制作而成,钢管一端封闭,一端开口。As shown in FIG. 3 , in order to measure the temperature of the fluid at the center of the heat transfer tube 12 , several thermocouple traps 20 are arranged in the heat transfer tube 12 . The thermocouple trap is inserted into the heat transfer tube 12 and is silver-welded with the wall surface of the heat transfer tube 12 , and is supported at the center of the heat transfer tube 12 by a tripod bracket 21 . An armored thermocouple with a diameter of 0.5 mm is threaded through the open end of the thermocouple well 20 . According to the test data requirements, the test device needs to arrange 10 thermocouples in the A heat transfer tube 12, 12 thermocouples in the B heat transfer tube 12, and 13 thermocouples in the C heat transfer tube 12. The selection of the size of the thermocouple trap should not only ensure that a sufficient number of thermocouples can be penetrated, but also minimize its influence on the fluid flow in the heat transfer tube. At the same time, it must also meet the design conditions of 20MPa and 350°C. Therefore, the thermocouple well 20 is made of Φ3×0.5 mm 304 stainless steel seamless pipe, one end of the steel pipe is closed and the other end is open.
传热管12外壁面温度使用直接焊接在外壁表面的热电偶进行测量。A管表面布置了10根热电偶,B管布置了14根,C管布置了13根。壁面温度热电偶与中心流体温度热电偶交错分布。The temperature of the outer wall surface of the heat transfer tube 12 is measured by a thermocouple directly welded on the outer wall surface. There are 10 thermocouples arranged on the surface of tube A, 14 thermocouples on tube B, and 13 thermocouples on tube C. Wall temperature thermocouples and central fluid temperature thermocouples are distributed alternately.
此外,为测量冷却水箱13池水温度,在冷却水箱13中布置了18根热偶阱。热偶阱插入冷却水箱13中,并与水箱壁面焊接。直径为0.5mm的铠装热电偶穿进热偶阱中,每个热偶阱中安装1根热电偶。In addition, in order to measure the pool water temperature of the cooling water tank 13, 18 thermocouple traps are arranged in the cooling water tank 13. The thermocouple trap is inserted into the cooling water tank 13 and welded with the wall of the water tank. Armored thermocouples with a diameter of 0.5mm penetrate into the thermocouple wells, and one thermocouple is installed in each thermocouple well.
(2)稳压器(2) Regulator
试验装置中稳压器2与传热试验段1的出口管道和屏蔽泵3的入口管道相连,其作用是维持主回路系统压力恒定,为回路系统提供足够的体积补偿,从而保证主回路系统的压力稳定性和安全性。In the test device, the pressurizer 2 is connected to the outlet pipe of the heat transfer test section 1 and the inlet pipe of the shielded pump 3, and its function is to maintain a constant pressure in the main loop system and provide sufficient volume compensation for the loop system, thereby ensuring the stability of the main loop system. Pressure stability and safety.
稳压器采用立式圆柱形结构,并且有上、下椭圆形封头,容器外壳用304不锈钢制成。稳压器稳压过程中,容器内气体排放由排气阀实现,排气阀安装在稳压器的顶端;系统压力保护通过安装在稳压器上端的安全阀实现,当压力超过19MPa时,安全阀开启,当压力下降到18MPa时,安全阀自动回座密封,保持主回路系统的压力在额定范围内运行。稳压器主要技术参数见表4。The voltage stabilizer adopts a vertical cylindrical structure, and has upper and lower oval heads, and the container shell is made of 304 stainless steel. During the voltage stabilization process of the voltage stabilizer, the gas discharge in the container is realized by the exhaust valve, which is installed on the top of the voltage stabilizer; the system pressure protection is realized by the safety valve installed on the upper end of the voltage stabilizer. When the pressure exceeds 19MPa, The safety valve opens, and when the pressure drops to 18MPa, the safety valve will automatically return to its seat and seal to keep the pressure of the main circuit system operating within the rated range. The main technical parameters of the regulator are shown in Table 4.
表4稳压器主要技术参数Table 4 main technical parameters of the regulator
(3)屏蔽泵(3) Canned pump
屏蔽泵3与传热试验段1的出口管道相连,是主回路循环系统的主要动力设备,提供不同试验工况下所需的流体流量。当进行较大流量的循环传热试验时,自然循环达不到试验工况所需流量,就需要开启屏蔽泵3进行强迫循环传热试验。通过调节屏蔽泵3前的阀门VAJ102和旁通阀门VAJ101,调节主回路的流量。The shielded pump 3 is connected to the outlet pipe of the heat transfer test section 1, and is the main power equipment of the main circuit circulation system, providing the required fluid flow under different test conditions. When carrying out the cyclic heat transfer test with a large flow rate, if the natural circulation cannot reach the required flow rate of the test working condition, it is necessary to turn on the canned pump 3 to carry out the forced cycle heat transfer test. By adjusting the valve VAJ102 and the bypass valve VAJ101 in front of the canned pump 3, the flow of the main circuit is adjusted.
根据试验装置的设计能力定位,需要主回路循环系统具备15m3/h的循环流量能力。因此,选取屏蔽泵3的主要技术参数见表5。屏蔽泵3与主回路管道采用焊接形式连接。泵的轴承润滑及屏蔽套的冷却通过二次水循环冷却系统来保证。泵的轴承润滑、屏蔽套冷却用的冷却水必须保证连续供应,当冷却水中断时,控制系统报警,并切断屏蔽泵3电源。According to the design capacity orientation of the test device, the circulation system of the main loop is required to have a circulation flow capacity of 15m 3 /h. Therefore, the main technical parameters of the selected canned pump 3 are shown in Table 5. The canned pump 3 is connected to the main circuit pipeline by welding. The bearing lubrication of the pump and the cooling of the shielding sleeve are guaranteed by the secondary water circulation cooling system. The cooling water used for lubricating the bearings of the pump and cooling the shielding sleeve must ensure continuous supply. When the cooling water is interrupted, the control system will alarm and cut off the power supply of the shielding pump 3.
表5主循环泵技术参数Table 5 Main Circulation Pump Technical Parameters
(4)加热器(4) Heater
加热器4安装在屏蔽泵2和传热试验段1之间,主回路流体流经加热器4,再经上分流器14流入传热管12。通过调节加热器4的功率,使传热管12入口温度达到试验要求。The heater 4 is installed between the shielded pump 2 and the heat transfer test section 1 , the main circuit fluid flows through the heater 4 , and then flows into the heat transfer pipe 12 through the upper splitter 14 . By adjusting the power of the heater 4, the inlet temperature of the heat transfer tube 12 can meet the test requirements.
加热器4最大工作压力为15MPa,最大工作温度为324℃。加热器内工质为纯水。加热器4采用Φ32×3mm、长度约4.5m的管子制成。加热器4与主回路管道通过法兰连接,法兰间加绝缘密封垫片。加热器4采用经可控硅整流电源整定后的直流低电压大电流直接输出到加热管段上的加热方式。整流电源输出为12脉波直流DC:50V、0~10000A。加热电功率为300KW。管道中间接电源正极,两端接电源负极。The maximum working pressure of the heater 4 is 15MPa, and the maximum working temperature is 324°C. The working fluid in the heater is pure water. The heater 4 is made of a pipe with a diameter of Φ32×3mm and a length of about 4.5m. The heater 4 is connected to the main circuit pipeline through flanges, and insulating sealing gaskets are added between the flanges. The heater 4 adopts a heating method in which the DC low voltage and high current regulated by the silicon controlled rectifier power supply are directly output to the heating pipe section. The output of the rectified power supply is 12-pulse DC: 50V, 0-10000A. The heating electric power is 300KW. The middle of the pipeline is connected to the positive pole of the power supply, and the two ends are connected to the negative pole of the power supply.
(5)循环泵(5) Circulation pump
循环泵5为离心泵,其入口与换热器6的管程出口连接,出口与冷却水箱13的入口管16相连,其作用是将冷却水箱13内的水抽出,经换热器6冷却后,再注入冷却水箱13,实现冷却水箱13内水的循环和温度恒定。The circulation pump 5 is a centrifugal pump, its inlet is connected to the outlet of the tube side of the heat exchanger 6, and its outlet is connected to the inlet pipe 16 of the cooling water tank 13. , and then injected into the cooling water tank 13 to realize the circulation and constant temperature of the water in the cooling water tank 13 .
(6)换热器(6) Heat exchanger
换热器6的管程入口与冷却水箱13的出口管18相连,管程出口与循环泵5的入口相连,其作用是降低从冷却水箱13出来的流体温度,以实现冷却水箱13内水温恒定。换热器为蒸发式换热器,采用管壳式结构,立式布置,管程换热管采用U型布置。壳程为圆柱筒体结构,筒体与上下封头连接,上封头为椭圆形封头,下封头为球形封头。壳程和管程材质均为304不锈钢。换热器6的主要技术参数见表6。The tube-side inlet of the heat exchanger 6 is connected to the outlet pipe 18 of the cooling water tank 13, and the tube-side outlet is connected to the inlet of the circulation pump 5, and its function is to reduce the temperature of the fluid coming out of the cooling water tank 13, so as to realize constant water temperature in the cooling water tank 13 . The heat exchanger is an evaporative heat exchanger with a shell-and-tube structure and a vertical arrangement, and the tube-side heat exchange tubes are arranged in a U-shape. The shell side is a cylinder structure, the cylinder is connected with the upper and lower heads, the upper head is an elliptical head, and the lower head is a spherical head. Shell side and tube side are made of 304 stainless steel. The main technical parameters of the heat exchanger 6 are shown in Table 6.
表6换热器技术参数表Table 6 Heat Exchanger Technical Parameters
(7)高位水箱(7) High water tank
高位水箱7的功能是储存主回路系统用纯水,在重力作用下向主回路系统注水。高位水箱为直径1m、高1.2m的圆柱形水箱。水箱工作温度为20~90℃,工作压力为常压,水箱材质为304不锈钢。The function of the high level water tank 7 is to store the pure water for the main circuit system, and inject water to the main circuit system under the action of gravity. The high-level water tank is a cylindrical water tank with a diameter of 1m and a height of 1.2m. The working temperature of the water tank is 20-90°C, the working pressure is normal pressure, and the material of the water tank is 304 stainless steel.
(8)低位水箱(8) Low water tank
低位水箱8的功能是储存主回路系统用纯水。低位水箱为1×1×1.3m的立方体水箱。水箱工作温度为20~90℃,工作压力为常压,水箱材质为304不锈钢。The function of the low water tank 8 is to store pure water for the main circuit system. The low-level water tank is a cubic water tank of 1×1×1.3m. The working temperature of the water tank is 20-90°C, the working pressure is normal pressure, and the material of the water tank is 304 stainless steel.
(9)提升泵(9) lift pump
提升泵9与高位水箱7和低位水箱8相连,其作用是将低位水箱8中的水注入高位水箱7中。高位储水箱和低位储水箱的液位差约10m。因此,采用立式不锈钢离心泵HS50-250A,额定扬程为70m,额定流量为20m3/h。The lifting pump 9 is connected with the high water tank 7 and the low water tank 8, and its effect is to inject the water in the low water tank 8 into the high water tank 7. The liquid level difference between the high level water storage tank and the low level water storage tank is about 10m. Therefore, a vertical stainless steel centrifugal pump HS50-250A is adopted, with a rated head of 70m and a rated flow of 20m 3 /h.
(10)补水泵(10) Make-up water pump
补水泵10安装在低位水箱8和稳压器2下管口之间,其作用是将低位水箱中的水从稳压器2底部注入,提升稳压罐压力,且保证稳压器2内的水面不低于最低液位值。补水泵10流量为60L/h。The supplementary water pump 10 is installed between the lower water tank 8 and the lower nozzle of the pressurizer 2, and its effect is to inject the water in the lower water tank from the bottom of the pressurizer 2 to enhance the pressure of the pressurized tank and ensure the water in the pressurizer 2. The water level is not lower than the minimum liquid level value. The flow rate of the supplementary water pump 10 is 60L/h.
(11)喷淋泵(11)Spray pump
喷淋泵11安装在低位水箱8和稳压器2上管口之间,其作用是将低位水箱中的水通过稳压器2顶部喷淋装置向稳压器2中注水,以降低蒸汽温度。喷淋泵11流量为60L/h。The spray pump 11 is installed between the low-level water tank 8 and the upper nozzle of the pressurizer 2, and its function is to inject water from the low-level water tank into the pressurizer 2 through the spray device on the top of the pressurizer 2 to reduce the steam temperature . The spray pump 11 flow rate is 60L/h.
本发明的操作方法如下:在自然循环试验开始前,关闭阀门VAJ101和VAJ102,将屏蔽泵从试验回路中隔离开。确保VCO103阀门开启。开启阀门VHO202和VHO203,启动提升泵将低位水箱中的水提升到高位水箱中。当高位水箱溢流时,关闭提升泵和阀门VHO203、VHO201。打开阀门VHO105,VHO104和VHO204,向包含稳压罐、冷却水箱和主管道在内的试验回路灌水。The operation method of the present invention is as follows: before the natural circulation test starts, the valves VAJ101 and VAJ102 are closed to isolate the canned pump from the test circuit. Make sure the VCO103 valve is open. Open the valves VHO202 and VHO203, start the lift pump to lift the water in the low water tank to the high water tank. When the high water tank overflows, close the lift pump and valves VHO203 and VHO201. Open the valves VHO105, VHO104 and VHO204, and fill the test circuit including the surge tank, cooling water tank and main pipeline with water.
当试验回路中充满水时,关闭阀门VHO105。向稳压罐中充入氮气,然后开启补水泵给主回路增压,直到达到试验所需压力。开启加热器加热主回路中的水。当主回路中的水流经加热器时,温度上升导致密度下降,于是向上流动进入试验段。调节加热器功率和VCO103的开度,使得试验段的入口水温达到试验条件。当热水流经试验段时,被冷却水箱所冷却,密度增加,于是向下流动,流出试验段,并经主管道回到加热器中。这一过程就在主回路中形成了自然循环。When the test circuit is full of water, close the valve VHO105. Fill nitrogen into the surge tank, and then turn on the make-up water pump to pressurize the main circuit until the pressure required for the test is reached. Turn on the heater to heat the water in the main circuit. As the water in the main circuit flows through the heater, the temperature rises causing the density to drop and it flows up into the test section. Adjust the heater power and the opening of VCO103 so that the inlet water temperature of the test section reaches the test conditions. When hot water flows through the test section, it is cooled by the cooling water tank, and its density increases, so it flows downward, out of the test section, and returns to the heater through the main pipe. This process forms a natural cycle in the main loop.
与此同时,开启循环泵使得冷却水箱中的水通过换热器循环,开启阀门VHO303和VHO304,使得换热器的二次水循环来冷却水箱中的水。At the same time, turn on the circulation pump to make the water in the cooling water tank circulate through the heat exchanger, and open the valves VHO303 and VHO304 to make the secondary water of the heat exchanger circulate to cool the water in the water tank.
当系统达到稳定状态时,计算机开始记录试验数据,每秒钟记录一次,包括传热管内温度、管壁温度、水箱温度、流速和加热功率等。When the system reaches a steady state, the computer starts to record the test data every second, including the temperature inside the heat transfer tube, the temperature of the tube wall, the temperature of the water tank, the flow rate and the heating power, etc.
如果需要进行强迫循环试验,则打开阀门VAJ101和VAJ102。其他操作方法与自然循环试验的操作方法相同。开启屏蔽泵,通过调节VAJ101和VAJ102的开度,对主回路的流量进行调节,以满足试验工况的流量要求。If forced circulation test is required, open valves VAJ101 and VAJ102. Other operating methods are the same as those of the natural circulation test. Turn on the canned pump, and adjust the flow of the main circuit by adjusting the opening of VAJ101 and VAJ102 to meet the flow requirements of the test conditions.
显然,本领域的技术人员可以对本发明进行各种改动和变型而不脱离本发明的精神和范围。这样,倘若对本发明的这些修改和变型属于本发明权利要求及其同等技术的范围之内,则本发明也意图包含这些改动和变型在内。Obviously, those skilled in the art can make various changes and modifications to the present invention without departing from the spirit and scope of the present invention. Thus, if these modifications and variations of the present invention fall within the scope of the claims of the present invention and equivalent technologies, the present invention also intends to include these modifications and variations.
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CN104952497A (en) * | 2015-06-29 | 2015-09-30 | 中国原子能科学研究院 | Passive residual heat removal heat exchanger testing device |
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CN104952497A (en) * | 2015-06-29 | 2015-09-30 | 中国原子能科学研究院 | Passive residual heat removal heat exchanger testing device |
CN106024079A (en) * | 2016-08-02 | 2016-10-12 | 合肥通用机械研究院 | Passive residual heat removal circulation performance test system and test method |
CN108231223A (en) * | 2016-08-02 | 2018-06-29 | 合肥通用机械研究院 | A kind of passive residual heat removal cycle performance test method |
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