CN105225710B - The reactor core analogue body and steam generator analogue body method for designing of circulation loop system - Google Patents

The reactor core analogue body and steam generator analogue body method for designing of circulation loop system Download PDF

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CN105225710B
CN105225710B CN201510531962.4A CN201510531962A CN105225710B CN 105225710 B CN105225710 B CN 105225710B CN 201510531962 A CN201510531962 A CN 201510531962A CN 105225710 B CN105225710 B CN 105225710B
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analogue body
steam generator
reactor core
design
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刘艳军
黄志强
袁娇
吴国凤
何霞
马欣
于春雨
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Southwest Petroleum University
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Abstract

本发明公开了一种循环回路系统的堆芯模拟体和蒸汽发生器模拟体设计方法,包括堆芯模拟体的设计要求、结构设计、相似比例分析和设计,以及蒸汽发生器模拟体的设计要求、结构设计和设计结果,该方法根据自然循环实验回路的设计参数和功能需求,确定实验回路系统堆芯模拟体和蒸汽发生器模拟体的设计要求,再分别对堆芯模拟体和蒸汽发生器模拟体进行设计和分析计算。本发明提高了超设计基准事故设置的措施的可靠性和核电厂安全系统的多样化,具有很高的工程价值。

The invention discloses a method for designing a reactor core simulation body and a steam generator simulation body of a circulation loop system, including design requirements, structural design, similarity ratio analysis and design of the reactor core simulation body, and design requirements of the steam generator simulation body , structural design and design results, this method determines the design requirements of the core simulation body and the steam generator simulation body of the experimental loop system according to the design parameters and functional requirements of the natural circulation experimental loop, and then respectively determines the core simulation body and the steam generator simulation body The simulation body is designed and analyzed. The invention improves the reliability of the measures for accident setting beyond the design basis and the diversification of the safety system of the nuclear power plant, and has high engineering value.

Description

循环回路系统的堆芯模拟体和蒸汽发生器模拟体设计方法Design Method of Core Simulator and Steam Generator Simulator for Circulation Loop System

技术领域technical field

本发明属于反应堆热工水利领域,尤其涉及一种循环回路系统的堆芯模拟体和蒸汽发生器模拟体设计方法。The invention belongs to the field of reactor thermal water conservancy, and in particular relates to a design method for a core simulation body and a steam generator simulation body of a circulation loop system.

背景技术Background technique

反应堆可以利用自然循环不依赖外部动力就将热量导出的能力,实现反应堆非能动安全设施在事故下的运行,从而提高反应堆的安全性。The reactor can use the ability of natural circulation to export heat without relying on external power to realize the operation of the passive safety facilities of the reactor under accidents, thereby improving the safety of the reactor.

自日本福岛事件后,国际和国内社会对核能安全提出了更高的要求,特别针对全厂断电和完全丧失冷却链等超设计基准事故缓解措施的可靠性给予了越来越多的关注。2012年6月国家核安全局对外发布的《福岛核事故后核电厂改进行动通用技术要求(试行)》中,多次提出对在运和在建核电机组在核电厂部分或全部安全系统功能丧失的情况下,如超设计基准洪水事件条件下,应该采取更多措施以带出余热。新近发布的《“十二五”期间新建核电厂安全要求和审评原则》中,明确要求十二五期间新建核电厂须增加反应堆堆芯的余热排出、应急冷却和最终热阱的考虑,应设置多样化的最终热阱。Since the Fukushima incident in Japan, the international and domestic communities have put forward higher requirements for nuclear energy safety, and more and more attention has been paid to the reliability of mitigation measures for beyond-design basis accidents such as power outages and complete loss of cooling chains. . In the "General Technical Requirements for Nuclear Power Plant Improvement Actions after the Fukushima Nuclear Accident (Trial)" issued by the National Nuclear Safety Administration in June 2012, it has repeatedly proposed that some or all of the safety system functions of nuclear power units in operation and under construction in nuclear power plants In the case of loss, such as the flood event beyond the design basis, more measures should be taken to bring out the residual heat. The newly released "Safety Requirements and Review Principles for New Nuclear Power Plants During the Twelfth Five-Year Plan Period" clearly requires that new nuclear power plants during the Twelfth Five-Year Plan period must increase the consideration of waste heat discharge from the reactor core, emergency cooling and final heat sink. Set up a diverse final heat sink.

ACPR1000项目目前的技术方案,尽管已经针对超设计基准事故设置了一些缓解措施,但在核电厂安全系统多样化设计方面尚有较大欠缺。根据目前确定论安全分析和PSA分析结果,蒸汽发生器二次侧相关事故具有重大贡献。因此,需要针对完全丧失给水、主蒸汽管道破裂及主给水管道破裂叠加辅助给水丧失、全厂断电、完全丧失冷却链等超设计基准事故设置可靠性更高的多样化缓解系统,而二次侧非能动余热排除系统正符合该要求。本发明正是针对上述问题而设计。Although the current technical scheme of the ACPR1000 project has set up some mitigation measures for beyond design basis accidents, there is still a big gap in the diversification design of the safety system of the nuclear power plant. According to the results of the current deterministic safety analysis and PSA analysis, the accidents related to the secondary side of the steam generator have a significant contribution. Therefore, it is necessary to set up a diversified mitigation system with higher reliability for accidents beyond the design basis such as complete loss of feed water, rupture of main steam pipe, rupture of main feed water pipe combined with loss of auxiliary feed water, power outage of the whole plant, complete loss of cooling chain, etc. The side passive waste heat removal system meets this requirement. The present invention is designed at the above-mentioned problem just.

发明内容Contents of the invention

本发明实施例的目的在于提供一种循环回路系统的堆芯模拟体和蒸汽发生器模拟体设计方法,旨在解决对超设计基准事故设置的措施可靠性不够高,核电厂安全系统多样化存在较大欠缺的问题。The purpose of the embodiments of the present invention is to provide a design method for the core simulation body and the steam generator simulation body of the circulation loop system, aiming at solving the problem that the reliability of the measures set for accidents beyond the design basis is not high enough, and the safety systems of nuclear power plants are diversified. The problem of major deficiencies.

本发明是这样实现的,一种循环回路系统的堆芯模拟体和蒸汽发生器模拟体设计方法,包括堆芯模拟体的设计要求、结构设计、相似比例分析和设计,以及蒸汽发生器模拟体的设计要求、结构设计和设计结果,该方法根据自然循环实验回路的设计参数和功能需求,确定实验回路系统堆芯模拟体和蒸汽发生器模拟体的设计要求,再分别对堆芯模拟体和蒸汽发生器模拟体进行设计和分析计算。The present invention is achieved in this way, a method for designing a core simulation body and a steam generator simulation body of a circulation loop system, including the design requirements, structural design, similarity ratio analysis and design of the reactor core simulation body, and the steam generator simulation body According to the design requirements, structural design and design results of the natural circulation experimental circuit, this method determines the design requirements of the core simulation body and the steam generator simulation body of the experimental loop system, and then respectively determines the core simulation body and the steam generator simulation body. The steam generator simulation body is designed and analyzed.

进一步,堆芯模拟体的设计以ACPR1000为原型,ACPR1000堆芯有157盒燃料组件,该堆芯模拟体模拟其中的一盒燃料组件,高度比取1:4,速度比为1:2,电加热元件的表面热流密度比为2:1;Furthermore, the design of the core simulation body is based on ACPR1000 as the prototype. The ACPR1000 core has 157 boxes of fuel assemblies. The core simulation body simulates one of the fuel assemblies. The surface heat flux ratio of the heating element is 2:1;

堆芯模拟体包括铜棒、平盖、筒体端部、进出口接头、进出口法兰、筒体、吊篮、陶瓷、燃料组件模拟件、下封头、挂环、进出口反法兰;The core simulation body includes copper rods, flat covers, cylinder ends, inlet and outlet joints, inlet and outlet flanges, cylinders, hanging baskets, ceramics, fuel assembly simulation parts, lower heads, hanging rings, inlet and outlet anti-flanges ;

燃料组件模拟件通过吊篮悬挂于挂环上,平盖上装有2根铜棒,铜棒中的两根铜棒一端分别和电源的正负极相连,另一端与燃料组件模拟件相连;The fuel assembly simulation part is suspended on the hanging ring through the hanging basket. Two copper rods are installed on the flat cover. One end of the two copper rods is connected to the positive and negative poles of the power supply, and the other end is connected to the fuel assembly simulation part;

组件模拟件和金属吊篮之间用陶瓷填充。The space between the component mock-up and the metal hanging basket is filled with ceramics.

进一步,堆芯模拟体堆芯模拟体管道用长度、水力学当量直径和流通截面积体现其流速、流动阻力。Further, the length, hydraulic equivalent diameter, and flow cross-sectional area of the core simulation body piping of the core simulation body reflect its flow velocity and flow resistance.

进一步,堆芯模拟体设计中的无量纲动量方程为:Furthermore, the dimensionless momentum equation in the design of the core simulation volume is:

无量纲能量方程为:The dimensionless energy equation is:

动量和能量方程中无量纲参数的定义分别为:Richardson数表征浮升力与惯性力之间的关系;阻力系数表征回路的摩擦和形阻;热源数也称相变数表征燃料元件释热对回路焓升的影响;热容数表征结构的热容量与回路焓升的关系。The definitions of the dimensionless parameters in the momentum and energy equations are respectively: Richardson number Characterizes the relationship between buoyancy and inertial forces; drag coefficient Characterize the friction and shape resistance of the circuit; the heat source number is also called the phase change number Characterize the effect of fuel element heat release on loop enthalpy rise; heat capacity numbers Characterize the heat capacity of a structure as a function of loop enthalpy rise.

进一步,堆芯模拟体设计中的无量纲相变数为:Furthermore, the dimensionless phase transition number in the design of the core simulation volume is:

无量纲过冷度数为:The dimensionless degree of supercooling is:

进一步,蒸汽发生器模拟体对蒸汽发生器进行模化,换热管高度比取1:4,采用原型的换热管径以及栅距,蒸汽发生器一次侧和二次侧的温度和压力都与原型一致,根据原型中蒸汽发生器的换热能力和换热面积,模化得到实验回路中蒸汽发生器的换热面积及换热管的结构尺寸;Furthermore, the steam generator simulation body models the steam generator, the heat exchange tube height ratio is 1:4, the heat exchange tube diameter and grid pitch of the prototype are adopted, the temperature and pressure of the primary side and the secondary side of the steam generator are both Consistent with the prototype, according to the heat transfer capacity and heat transfer area of the steam generator in the prototype, the heat transfer area of the steam generator in the experimental circuit and the structural size of the heat transfer tube are obtained by modeling;

蒸汽发生器模拟体包括上封头、端壳体、换热管、下端壳体、下封头,换热管通过固定管板固定于下端壳体上,换热管的不同位置装有足够数量的支撑板和挡板,下封头被隔板隔开隔开。The steam generator simulation body includes an upper head, an end shell, a heat exchange tube, a lower end shell, and a lower end head. The heat exchange tube is fixed on the lower end shell through a fixed tube sheet, and sufficient quantities of The supporting plate and the baffle, and the lower head is separated by a partition.

进一步,堆芯模拟体采用长1050mm,外径9.5mm的不锈钢管作为加热元件,电加热元件采用定位格架固定,定位格架拟采用原型中的定位格架,电加热元件的上下端和铜板相连,铜板分别和电源的正负极相连,堆芯模拟体的进出口管道用内径为105mm的不锈钢管,位置按原型布置,电加热元件和压力容器之间用陶瓷填充。Further, the core simulation body adopts a stainless steel tube with a length of 1050 mm and an outer diameter of 9.5 mm as a heating element, and the electric heating element is fixed by a positioning grid, and the positioning grid is planned to adopt the positioning grid in the prototype, and the upper and lower ends of the electric heating element and the copper plate The copper plates are respectively connected to the positive and negative poles of the power supply. The inlet and outlet pipes of the core simulation body are stainless steel pipes with an inner diameter of 105mm. The positions are arranged according to the prototype, and the space between the electric heating element and the pressure vessel is filled with ceramics.

本发明提高了超设计基准事故设置的措施的可靠性和核电厂安全系统的多样化,具有很高的工程价值。The invention improves the reliability of the measures for accident setting beyond the design basis and the diversification of the safety system of the nuclear power plant, and has high engineering value.

附图说明Description of drawings

图1是本发明实施例提供的堆芯模拟体主视图;Fig. 1 is the front view of the core simulation body provided by the embodiment of the present invention;

图2是本发明实施例提供的堆芯模拟体进出口管府视图;Fig. 2 is a view of the inlet and outlet pipes of the core simulation body provided by the embodiment of the present invention;

图3是本发明实施例提供的堆芯模拟体管座俯视图;Fig. 3 is a top view of the base of the core simulation body provided by the embodiment of the present invention;

图4是本发明实施例提供的换热管布管示意图;Fig. 4 is a schematic diagram of the heat exchange tube layout provided by the embodiment of the present invention;

图5是本发明实施例提供的换热管布管的B-B向剖视图;Fig. 5 is a B-B cross-sectional view of the heat exchange tube layout provided by the embodiment of the present invention;

图中:1、铜棒;2、平盖;3、筒体端部;4、进出口接头;5、进出口法兰;6、筒体;7、吊篮;8、陶瓷;9、燃料组件模拟件;10、下封头;11、挂环;12、进出口反法兰;13、蒸汽出口接管;14、上封头;15、上端壳体;16、换热管;17、下端壳体;18、固定管板;19、下封头;20、隔板;21、去离子水进出口接管;22、自来水进口接管;23、去离子水进口;24、去离子水出口;25、自来水进口;26、蒸汽出口。In the figure: 1, copper rod; 2, flat cover; 3, cylinder end; 4, inlet and outlet joints; 5, inlet and outlet flanges; 6, cylinder; 7, hanging basket; 8, ceramics; 9, fuel Component simulation part; 10. Lower head; 11. Hanging ring; 12. Inlet and outlet anti-flange; 13. Steam outlet connection; 14. Upper head; 15. Upper shell; 16. Heat exchange tube; 17. Lower end Shell; 18, fixed tube plate; 19, lower head; 20, partition; 21, deionized water inlet and outlet connection; 22, tap water inlet connection; 23, deionized water inlet; 24, deionized water outlet; 25 , Tap water import; 26, Steam outlet.

具体实施方式detailed description

为了使本发明的目的、技术方案及优点更加清楚明白,以下结合实施例,对本本发明进行进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本本发明,并不用于限定本发明。In order to make the object, technical solution and advantages of the present invention more clear, the present invention will be further described in detail below in conjunction with the examples. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.

1、堆芯模拟体的设计要求1. Design requirements for core simulation body

堆芯模拟体是自然循环实验回路开展非能动余热排除实验研究的关键性设备之一。以ACPR1000为原型,ACPR1000堆芯有157盒燃料组件,本堆芯模拟体模拟其中的一盒燃料组件。高度比取1:4,速度比为1:2,电加热元件的表面热流密度比为2:1,并合理设计轴向和横向阻力特性。The core simulation body is one of the key equipment for the experimental research of passive waste heat removal in the natural circulation experimental circuit. Taking ACPR1000 as the prototype, the core of ACPR1000 has 157 boxes of fuel assemblies, and this core simulator simulates one box of fuel assemblies. The height ratio is 1:4, the speed ratio is 1:2, the surface heat flux density ratio of the electric heating element is 2:1, and the axial and lateral resistance characteristics are reasonably designed.

2、堆芯模拟体结构设计2. Structural design of core simulation body

堆芯模拟体结构总图如图1-图3所示。堆芯模拟体包括铜棒1、平盖2、筒体端部3、进出口接头4、进出口法兰5、筒体6、吊篮7、陶瓷8、燃料组件模拟件9、下封头10、挂环11、进出口反法兰12。The general structure diagram of the core simulation body is shown in Fig. 1-Fig. 3. The core simulation body includes copper rod 1, flat cover 2, cylinder end 3, inlet and outlet joints 4, inlet and outlet flanges 5, cylinder 6, hanging basket 7, ceramics 8, fuel assembly simulation parts 9, and lower head 10, hanging ring 11, import and export anti-flange 12.

所述燃料组件模拟件9采用长1050mm(燃料组件高度的1/4),外径9.5mm(燃料组件的外径)的不锈钢管作为加热元件。为模拟燃料组件的定位格架,电加热元件也采用定位格架固定,其定位格架拟采用原型中的定位格架。燃料组件模拟件9通过吊篮7悬挂于挂环11上,实现固定。平盖2上装有2根铜棒1,铜棒1中的两根铜棒一端分别和电源的正负极相连,另一端与燃料组件模拟件9相连,实现电加热的目的。The fuel assembly simulation part 9 uses a stainless steel tube with a length of 1050 mm (1/4 of the height of the fuel assembly) and an outer diameter of 9.5 mm (the outer diameter of the fuel assembly) as a heating element. In order to simulate the spacer grid of the fuel assembly, the electric heating element is also fixed by the spacer grid, and the spacer grid is proposed to adopt the spacer grid in the prototype. The fuel assembly simulation part 9 is suspended on the hanging ring 11 through the hanging basket 7 to realize fixing. Two copper rods 1 are installed on the flat cover 2, and one end of the two copper rods 1 is respectively connected with the positive and negative poles of the power supply, and the other end is connected with the fuel assembly simulation part 9 to realize the purpose of electric heating.

为减小金属热容,组件模拟件9和金属吊篮7之间用陶瓷8填充。进出口接头4采用用内径为105mm的不锈钢管(约原型尺寸的1/7),且位置按原型布置。In order to reduce the heat capacity of the metal, ceramics 8 are used to fill the space between the component simulation part 9 and the metal hanging basket 7 . The inlet and outlet joint 4 adopts a stainless steel pipe (about 1/7 of the prototype size) with an internal diameter of 105mm, and the position is arranged according to the prototype.

3、堆芯模拟体相似比例分析3. Similar proportion analysis of core simulation body

反应堆一回路系统结构复杂,不论是堆芯还是蒸汽发生器,都需要通过一定的假设进行简化。反应堆一回路系统的设备可以简单的分为两种类型,即有热量传递和无热量传递;三种设备:管路、蒸汽发生器、堆芯。其中,此处的蒸汽发生器是指发生了进出口温度或密度变化的那部分,即蒸汽发生器管束。而反应堆堆芯则是发生了温度或密度变化的那部分堆芯,即加热部分,其余部分则视为管道。如果考虑到两相流型的影响,严格的说管道内流体的密度也可以发生变化。管道的特征是没有热量传递,只是流体的位置发生变化,并贡献阻力。反应堆管束中,如冷管和热管,在符合一维假设方面没有什么大的问题,而一些局部有突变的构件可以通过阻力作用来体现其在自然循环过程中的作用。因此,管道可以用长度、水力学当量直径和流通截面积体现其流速、流动阻力;通过在重力方向的投影体现其位置变化对重力作用的贡献。不论是几根管道,均可以一维化为上述特征的元件。The structure of the reactor primary loop system is complex, and both the core and the steam generator need to be simplified through certain assumptions. The equipment of the reactor primary loop system can be simply divided into two types, that is, with heat transfer and without heat transfer; three types of equipment: piping, steam generator, and core. Wherein, the steam generator here refers to the part where the inlet and outlet temperature or density changes, that is, the steam generator tube bundle. The reactor core is the part of the core that undergoes temperature or density changes, that is, the heated part, and the rest is considered the pipe. If the influence of the two-phase flow pattern is considered, strictly speaking, the density of the fluid in the pipeline can also change. Pipes are characterized by no heat transfer, only the fluid's position changes and contributes to resistance. In reactor tube bundles, such as cold pipes and heat pipes, there is no major problem in conforming to the one-dimensional assumption, while some components with local mutations can reflect their role in the natural circulation process through resistance. Therefore, the length, hydraulic equivalent diameter, and flow cross-sectional area of the pipeline can reflect its flow velocity and flow resistance; the contribution of its position change to the gravity can be reflected through the projection in the direction of gravity. Regardless of the number of pipes, they can be converted into one-dimensional components with the above features.

3.1基本方程3.1 Fundamental equations

首先是一维假设,认为流动沿着设备或管道的轴向方向进行,而传热则在一维边界的径向进行;其次,可以通过采用特征参数,如热工水力直径等方法,对径向影响的作用进行评估并进行模拟;此外,还需要忽略热损失、轴向传热及方程中的高阶项,其控制方程为:The first is the one-dimensional assumption, which means that the flow is carried out along the axial direction of the equipment or pipeline, while the heat transfer is carried out in the radial direction of the one-dimensional boundary; secondly, by using characteristic parameters, such as thermal hydraulic diameter, etc. The role of directional influence is evaluated and simulated; in addition, heat loss, axial heat transfer, and higher-order terms in the equation need to be ignored, and the governing equation is:

(1)连续性方程(1) Continuity equation

上式中ρ为流体密度,u为流体流速。In the above formula, ρ is the fluid density, and u is the fluid velocity.

(2)动量方程(2) Momentum equation

上式中P为压力,f为阻力系数,De为水力学当量直径。In the above formula, P is the pressure, f is the resistance coefficient, and De is the hydraulic equivalent diameter.

(3)能量方程(3) Energy equation

上式中h为流体的焓,ζ为周长,A为截面积,Tw和Tf分别为壁面温度和流体温度。In the above formula, h is the enthalpy of the fluid, ζ is the perimeter, A is the cross-sectional area, T w and T f are the wall temperature and fluid temperature, respectively.

(4)传热方程(4) Heat transfer equation

本发明对流换热系数不进行模拟,主要原因有:①金属构件结构复杂,本模型中的一维方法模拟不能准确描述;②两相传热温差很小,测量到的壁温不具有很大的价值;③燃料元件基本上是定热流密度传热,不受传热系数的影响,而燃料棒本身的壁温与材料、结构等有关,不必详细模拟,对其研究可以在其他情况下进行。这样,对基本方程中的能量方程和传热方程进行合并,其新的能量方程为:The present invention does not simulate the convective heat transfer coefficient, the main reasons are: 1. the structure of the metal member is complex, and the one-dimensional method simulation in this model cannot be accurately described; Value; ③The fuel element basically conducts heat with a constant heat flux and is not affected by the heat transfer coefficient, while the wall temperature of the fuel rod itself is related to the material and structure, so it is not necessary to simulate in detail, and its research can be carried out in other situations. In this way, the energy equation and the heat transfer equation in the basic equation are combined, and the new energy equation is:

将能量方程用质量含汽量表示Vapor content by mass express

3.2方程无量纲化3.2 Equation dimensionless

由能量方程(6)可知,回路流体的密度,主要受边界传热的控制。当堆芯传热有变化时,此时局部的密度发生变化,但该密度变化并不会立即对流速产生很大影响。只有该密度变化因流体流动传递到整个回路从而实质性的影响回路中的密度差,从而导致流速变化。因此,可以认为回路流体密度对于时间的偏微分项是一个可以忽略的项。因此,连续性方程变化为:It can be seen from the energy equation (6) that the density of the loop fluid is mainly controlled by the boundary heat transfer. When the core heat transfer changes, the local density changes at this time, but the density change does not immediately have a great impact on the flow rate. It is only this density change that substantially affects the density difference in the circuit as the fluid flow propagates throughout the circuit, resulting in a change in flow rate. Therefore, it can be considered that the partial differential term of the circuit fluid density with respect to time is an item that can be ignored. Therefore, the continuity equation changes to:

ρuA=ρinuinAin=const (7)ρuA = ρ in u in A in = const (7)

上式中ρin、uin和Ain分别为堆芯入口处的密度、流速和流通截面积。In the above formula, ρ in , u in and A in are the density, flow velocity and flow cross-sectional area at the inlet of the core, respectively.

将守恒方程无量纲化,其无量纲参数分别为:速度长度密度密度差流通面积时间温度等,其角标0代表参数的初始值。The conservation equation is dimensionless, and its dimensionless parameters are: velocity length density density difference circulation area time temperature etc., the subscript 0 represents the initial value of the parameter.

连续方程无量纲化:The continuity equation is dimensionless:

即无量纲速度为 That is, the dimensionless velocity is

动量方程无量纲化:The momentum equation is dimensionless:

(1)重力压降项Δρglhc (1) Gravity pressure drop term Δρgl hc

(2)惯性项 (2) Inertia term

可得 Depend on Available

(3)摩擦项 (3) Friction item

(4)迁移项 (4) Migration item

无量纲化后的动量方程为The momentum equation after dimensionless is

无量纲化后的能量方程为(推导方法与动量方程类似)The energy equation after dimensionless is (the derivation method is similar to the momentum equation)

动量和能量方程中无量纲参数的定义分别为:Richardson数表征浮升力与惯性力之间的关系;阻力系数表征回路的摩擦和形阻;热源数也称相变数表征燃料元件释热对回路焓升的影响;热容数表征结构的热容量与回路焓升的关系。The definitions of the dimensionless parameters in the momentum and energy equations are respectively: Richardson number Characterizes the relationship between buoyancy and inertial forces; drag coefficient Characterize the friction and shape resistance of the circuit; the heat source number is also called the phase change number Characterize the effect of fuel element heat release on loop enthalpy rise; heat capacity numbers Characterize the heat capacity of a structure as a function of loop enthalpy rise.

3.3相似准则3.3 Similarity criterion

首先确定高度比相似First make sure the height ratio is similar

为满足原型和模型之间相似,(14)和(15)式的模型和原型的比值均等于1,所以有In order to satisfy the similarity between the prototype and the model, the ratios of the model and the prototype in (14) and (15) are both equal to 1, so we have

为满足连续方程相似,有In order to satisfy the similarity of the continuity equation, we have

对于流动阻力,主要是因为气液两相流动模拟特性的需要,采用原型相同的棒束排列结构较为适宜。在相同介质(水-水模拟)且等压模拟中,首先,原型和模型的流通面积相似,即For the flow resistance, it is more appropriate to adopt the same rod bundle arrangement structure as the prototype because of the requirement of the gas-liquid two-phase flow simulation characteristics. In the same medium (water-water simulation) and isobaric simulation, first, the flow area of the prototype and the model is similar, that is

可得 Depend on and Available

根据式(23)有According to formula (23), we have

这个准则数表征原型和模型的压力比为定值:which is This criterion number characterizes the pressure ratio of the prototype and the model as a constant:

根据上式可以得到堆芯进出口密度存在以下关系According to the above formula, it can be obtained that the core inlet and outlet density has the following relationship

根据式(17)、式(24)和式(26)可以得到According to formula (17), formula (24) and formula (26), we can get

上式表达的是相同物性下高度比和自然循环速度比的关系。The above formula expresses the relationship between the height ratio and the natural circulation speed ratio under the same physical properties.

Fi)R据式(21)可以简化为:Fi ) R can be simplified according to formula (21):

由于模型和原型的压力比为定值,所以成立。Since the pressure ratio of the model and the prototype is constant, so established.

同样,可以将[(ΠH)i]R写成:Similarly, [(Π H ) i ] R can be written as:

该式就是无量纲相变数同理,由入口含气量的定义可以推导到无量纲过冷度数 This formula is the dimensionless phase change number In the same way, the definition of inlet air content can be deduced to the dimensionless subcooling degree

从能量方程得知,堆芯内的质量含气量变化相同,如果保证堆芯出口的含气量相等(Xe)R=1,则(Xin)R=1,有It is known from the energy equation that the mass gas content in the core changes the same, if the gas content at the core outlet is guaranteed to be equal (X e ) R =1, then (X in ) R =1, we have

sub)R=1 (30)sub ) R =1 (30)

对于热容数有:For heat capacity numbers there are:

上式在流体和金属材料的热物性相同时,有:When the thermophysical properties of the fluid and the metal material are the same, the above formula has:

该式表示在每一局部区域,金属构件与回路流体之间的质量关系。This formula represents the mass relationship between the metal component and the circuit fluid in each local area.

综上所述,等压水-水模拟准则关系如表1所示:In summary, the isobaric water-water simulation criterion relationship is shown in Table 1:

表1 等压水-水模拟准则数Table 1 Criteria for isobaric water-water simulation

3.4堆芯模拟体3.4 Core Simulator

本实验拟模拟一盒燃料组件,且原型中有157盒燃料组件,原型中堆芯入口流通截面积为由(22)式可得This experiment intends to simulate a box of fuel assemblies, and there are 157 boxes of fuel assemblies in the prototype, and the flow cross-sectional area of the core inlet in the prototype is From (22) can get

即模型中堆芯入口管径约为105mm。本实验中,直径比取1:7.23,面积比1:52,高度比取1:4,即速度比为1:2,电加热元件的表面热流密度比为2:1。堆芯模拟体的设计结果为:That is, the core inlet pipe diameter in the model is about 105mm. In this experiment, the diameter ratio is 1:7.23, the area ratio is 1:52, and the height ratio is 1:4, that is, the speed ratio is 1:2, and the surface heat flux ratio of the electric heating element is 2:1. The design results of the core simulation body are as follows:

a)堆芯高度1:4设计;a) Core height 1:4 design;

b)流通面积按照1:52设计,堆芯流速比为1:2;b) The flow area is designed according to 1:52, and the core flow rate ratio is 1:2;

c)采用直接加热方式,棒的表面热流密度比为2:1;c) Direct heating is adopted, and the surface heat flux density ratio of the rod is 2:1;

d)采用原型的棒直径,以及栅距;d) adopt the rod diameter of the prototype, and the grid pitch;

e)合理设计轴向和横向阻力特性(模拟定位格架);e) Reasonable design of axial and lateral resistance characteristics (simulation positioning grid);

f)适当模拟横向流动特性。f) Appropriate modeling of lateral flow characteristics.

4、蒸汽发生器设计要求4. Design requirements of steam generator

与堆芯模拟体类似,对蒸汽发生器进行模化,换热管高度比取1:4,采用原型的换热管径以及栅距。由模化可知,蒸汽发生器的热工参数尽应和原型保持一致,即蒸汽发生器一次侧和二次侧的温度和压力都应与原型一致。根据原型中蒸汽发生器的换热能力和换热面积,模化就可得到实验回路中蒸汽发生器的换热面积及换热管的结构尺寸。Similar to the core simulation body, the steam generator is modeled, the heat exchange tube height ratio is 1:4, and the heat exchange tube diameter and grid pitch of the prototype are adopted. It can be seen from the modeling that the thermal parameters of the steam generator should be consistent with the prototype, that is, the temperature and pressure of the primary side and the secondary side of the steam generator should be consistent with the prototype. According to the heat transfer capacity and heat transfer area of the steam generator in the prototype, the heat transfer area of the steam generator in the experimental circuit and the structural size of the heat transfer tube can be obtained by modeling.

5、蒸汽发生器结构设计5. Structural design of steam generator

如图4和5所示为蒸汽发生器结构设计图。蒸汽发生器包括上封头14、端壳体15、换热管16、下端壳体17、下封头19。去离子水由去离子水进出口23进入换热管16后与冷凝体换热,并由去离子水出口24流出,所述换热管16通过固定管板18固定于下端壳体17上,换热管16的不同位置应装有足够数量的支撑板和挡板,下封头19被隔板20隔开隔开。冷流体自来水由自来水进口25流入,流入后沉积在下端壳体17的空腔内与换热管16内的热流体发生热交换后气化为蒸汽,并由蒸汽出口26排出进行循环。Figures 4 and 5 show the structural design of the steam generator. The steam generator includes an upper head 14 , an end shell 15 , a heat exchange tube 16 , a lower end shell 17 , and a lower head 19 . The deionized water enters the heat exchange tube 16 from the deionized water inlet and outlet 23, exchanges heat with the condensate, and flows out from the deionized water outlet 24. The heat exchange tube 16 is fixed on the lower shell 17 through the fixed tube plate 18, Different positions of the heat exchange tubes 16 should be equipped with a sufficient number of support plates and baffles, and the lower heads 19 are separated by partitions 20 . The cold fluid tap water flows in through the tap water inlet 25, and after flowing in, deposits in the cavity of the lower shell 17 to exchange heat with the hot fluid in the heat exchange tube 16, then vaporizes into steam, and is discharged through the steam outlet 26 for circulation.

以上所述仅为本发明的较佳实施例而已,并不用以限制本发明,凡在本发明的精神和原则之内所作的任何修改、等同替换和改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements and improvements made within the spirit and principles of the present invention should be included in the protection of the present invention. within range.

Claims (6)

1. a kind of reactor core analogue body of circulation loop system and steam generator analogue body method for designing, it is characterised in that described Circulation loop system reactor core analogue body and steam generator analogue body method for designing including reactor core analogue body design requirement, Structure design, similar proportion analysis and design, and the design requirement of steam generator analogue body, structure design and design knot Really, the method determines experimental loop system heap core analogue body according to the design parameter and functional requirement of Natural Circulation experimental loop With the design requirement of steam generator analogue body, then reactor core analogue body and steam generator analogue body be designed and divided respectively Analysis is calculated;
With ACPR1000 as prototype, ACPR1000 reactor cores have 157 box fuel assemblies for the design of reactor core analogue body, the reactor core analogue body Box fuel assembly therein is simulated, highly than taking 1:4, speed ratio is 1:2, the surface heat flux ratio of electrical heating elements is 2: 1;
Reactor core analogue body includes copper rod, flat cover, barrel end, inlet-outlet connector, import and export flange, cylinder, hanging basket, ceramics, combustion Material component simulating piece, low head, link, the anti-flange of import and export;
Fuel assembly simulating piece, on link, is equipped with 2 copper rods, two copper rod one end in copper rod by hanging basket suspension on flat cover It is connected with the both positive and negative polarity of power supply respectively, the other end is connected with fuel assembly simulating piece;
Ceramic filler is used between component simulating piece and metal hanging basket.
2. the reactor core analogue body of circulation loop system as claimed in claim 1 and steam generator analogue body method for designing, its Be characterised by, reactor core analogue body reactor core analogue body pipeline length, hydraulics equivalent diameter and actual internal area embody its flow velocity, Flow resistance.
3. the reactor core analogue body of circulation loop system as claimed in claim 1 and steam generator analogue body method for designing, its It is characterised by, the dimensionless momentum equation in the design of reactor core analogue body is:
Π R Δρ + l h c + = Σ i l i + A i + ∂ u i n + ∂ τ + 1 2 ( u i n + ) 2 Π F + ( u i n + ) 2 Σ i ( A i n A i ) 2 ( ρ i n + ρ i + )
Dimensionless energy equation is:
( ρ + ρ i n + ) ∂ x ∂ τ + ∂ x ∂ s = Π p c h q + - Π C ∂ θ ∂ τ
The definition of dimensionless group is respectively in momentum and energy equation:Richardson numbersCharacterize buoyance lift Relation between power and inertia force;Resistance coefficientCharacterize friction and the shape in loop Resistance;Thermal source number is also referred to as phase parameterCharacterize the influence that fuel element heat release rises to loop enthalpy;Thermal capacitance numberCharacterize the relation that the thermal capacity of structure rises with loop enthalpy.
4. the reactor core analogue body of circulation loop system as claimed in claim 1 and steam generator analogue body method for designing, its It is characterised by, the dimensionless phase parameter in the design of reactor core analogue body is:
Π p c h = q 0 l h c 0 ξ i ρ 0 u 0 A 0 Δh f g ( Δρ f g ρ g )
Dimensionless is subcooled the number of degrees:
Π s u b = Δh s u b h f g ( Δρ f g ρ g ) .
5. the reactor core analogue body of circulation loop system as claimed in claim 1 and steam generator analogue body method for designing, its It is characterised by, steam generator analogue body carries out modelling to steam generator, tube height ratio takes 1:4, using changing for prototype The temperature and pressure of heat pipe footpath and pitch, primary side of steam generator and secondary side is all consistent with prototype, is steamed according in prototype The exchange capability of heat and heat exchange area of vapour generator, modelling obtains the heat exchange area and heat exchanger tube of steam generator in experimental loop Physical dimension;
Steam generator analogue body includes upper cover, end housing, heat exchanger tube, lower end housing, low head, and heat exchanger tube passes through fixing pipe Plate is fixed in lower end housing, and the diverse location of heat exchanger tube is sufficiently loaded with the supporting plate and baffle plate of quantity, low head by dividing plate every Open and separate.
6. the reactor core analogue body of circulation loop system as claimed in claim 1 and steam generator analogue body method for designing, its It is characterised by, reactor core analogue body uses 1050mm long, and the stainless steel tube of external diameter 9.5mm used as heating element heater, adopt by electrical heating elements Fixed with grid spacer, grid spacer is intended using the grid spacer in prototype, and the upper and lower side of electrical heating elements is connected with copper coin, copper Plate is connected with the both positive and negative polarity of power supply respectively, and the import and export pipeline internal diameter of reactor core analogue body is the stainless steel tube of 105mm, and position is pressed Prototype arrangement, uses ceramic filler between electrical heating elements and pressure vessel.
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