NGNP/HTE中热交换器占空比瞬态温度响应。

Richard B. Vilim
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First are the set of duty cycle transients over which the control engineer has little control but which none-the-less must be addressed. Second is the partitioning of the temperature response into a quasi-static component and a transient component. These two components are largely independent of each other and when addressed as such greater understanding of temperature change mechanisms and how to deal with them is achieved. Third is the manner in which energy and mass flow rates are managed. Generally one aims for a temperature distribution that minimizes spatial non-uniformity of thermal expansion in a component with time. This is can be achieved by maintaining a fixed spatial temperature distribution in a component during transients. A general rule of thumb for heat exchangers is to maintain flow rate proportional to thermal power. Additionally the product of instantaneous flow rate and heat capacity should be maintained the same on both sides of the heat exchanger. Fourth inherent mechanisms for stable behavior should not be compromised by active controllers that can introduce new feedback paths and potentially create under-damped response. Applications of these principles to the development of a plant control strategy for the reference NGNP/HTE plant can be found in the body of this report. The outcome is an integrated plant/control system design. The following conclusions are drawn from the analysis: (1) The plant load schedule can be managed to maintain near-constant hot side temperatures over the load range in both the nuclear and chemical plant. (2) The reactor open-loop response is inherently stable resulting mainly from a large Doppler temperature coefficient compared to the other reactivity temperature feedbacks. (3) The typical controller used to manage reactor power production to maintain reactor outlet temperature at a setpoint introduces a feedback path that tends to destabilize reactor power production in the NGNP. (4) A primary loop flow controller that forces primary flow to track PCU flow rate is effective in minimizing spatial temperature differentials within the IHX. (5) Inventory control in both the primary and PCU system during ramp load change transients is an effective means of maintaining high NGNP thermal efficiency while at reduced electric load. (6) Turbine bypass control is an effective means for responding to step changes in generator load when equipment capacity limitations prevent inventory control from being effective. (7) Turbine bypass control is effective in limiting PCU shaft over speed for the loss of generator load upset event. (8) The proposed control strategy is effective in limiting time variation of the differential spatial temperature distribution in the IHX during transients. Essentially the IHX can be made to behave in a manner where each point in the IHX experiences approximately the same temperature rate of change during a transient. (9) The stability of the closed-loop Brayton cycle was found to be sensitive to where one operates on the turbo-machine performance maps. There are competing interests: more stable operation means operating on the curves at points that reduce overall cycle efficiency. Future work should address in greater detail elements that came to light in the course of this work. Specifically: (1) A stability analysis should be performed to identify the phenomena that control reactor outlet temperature stability when operating with the Reactor Outlet Temperature Controller. The goal is to identify a better performing controller. (2) Future simulations should be performed with multiple axial nodes. The single axial node model for the core used in this work gives rise to an initial core reactor outlet temperature perturbation that is a numerical artifact. 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Applications of these principles to the development of a plant control strategy for the reference NGNP/HTE plant can be found in the body of this report. The outcome is an integrated plant/control system design. The following conclusions are drawn from the analysis: (1) The plant load schedule can be managed to maintain near-constant hot side temperatures over the load range in both the nuclear and chemical plant. (2) The reactor open-loop response is inherently stable resulting mainly from a large Doppler temperature coefficient compared to the other reactivity temperature feedbacks. (3) The typical controller used to manage reactor power production to maintain reactor outlet temperature at a setpoint introduces a feedback path that tends to destabilize reactor power production in the NGNP. (4) A primary loop flow controller that forces primary flow to track PCU flow rate is effective in minimizing spatial temperature differentials within the IHX. (5) Inventory control in both the primary and PCU system during ramp load change transients is an effective means of maintaining high NGNP thermal efficiency while at reduced electric load. (6) Turbine bypass control is an effective means for responding to step changes in generator load when equipment capacity limitations prevent inventory control from being effective. (7) Turbine bypass control is effective in limiting PCU shaft over speed for the loss of generator load upset event. (8) The proposed control strategy is effective in limiting time variation of the differential spatial temperature distribution in the IHX during transients. Essentially the IHX can be made to behave in a manner where each point in the IHX experiences approximately the same temperature rate of change during a transient. (9) The stability of the closed-loop Brayton cycle was found to be sensitive to where one operates on the turbo-machine performance maps. 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引用次数: 2

摘要

对与高温电解(HTE)厂对接的下一代核电厂(NGNP)进行了控制系统研究。温度变化和相关的热胁迫是决定植物寿命的重要因素。在NGNP中,中间热交换器(IHX) 40年使用寿命的设计目标尤其被视为一项挑战。设计了一个控制系统,以尽量减少IHX的温度变化,更广泛地说,在工厂的所有高温位置,用于占空比瞬变。在NGNP中,这包括反应堆出口和涡轮机进口的结构。这个问题是通过确定那些决定温度变化率的高级因素来解决的。首先是一组占空比暂态,控制工程师对其几乎没有控制能力,但仍然必须加以解决。其次是将温度响应划分为准静态分量和瞬态分量。这两个组成部分在很大程度上是相互独立的,当这样解决时,对温度变化机制和如何处理它们的更好理解就实现了。第三是管理能量和质量流率的方式。一般来说,人们的目标是使一个部件的热膨胀随时间的空间不均匀性最小化的温度分布。这可以通过在瞬态期间保持组件的固定空间温度分布来实现。热交换器的一般经验法则是保持流量与热功率成正比。另外,换热器两侧的瞬时流量与热容量的乘积应保持相同。第四,稳定行为的固有机制不应被主动控制器破坏,因为主动控制器可能引入新的反馈路径,并可能产生欠阻尼响应。在本报告的正文中可以找到这些原则在为参考NGNP/HTE工厂制定工厂控制战略方面的应用。其结果是一个集成的工厂/控制系统设计。分析得出以下结论:(1)核电站和化工厂的负荷计划都可以在负荷范围内保持热侧温度接近恒定。(2)与其他反应性温度反馈相比,反应器开环响应具有固有的稳定性,这主要是由于反应器的多普勒温度系数较大。(3)典型的用于管理反应堆功率生产以保持反应堆出口温度在一个设定值的控制器引入了一个反馈路径,该路径倾向于使NGNP中的反应堆功率生产不稳定。(4)主回路流量控制器强制主流量跟踪PCU流量,有效地减少了IHX内的空间温差。(5)在坡道负荷变化瞬态期间,主系统和PCU系统的库存控制是在减少电力负荷时保持高NGNP热效率的有效手段。(6)当设备容量限制使库存控制无法有效实施时,汽轮机旁通控制是应对发电机负荷阶跃变化的有效手段。(7)涡轮旁通控制能有效地限制PCU轴在发电机负荷失转情况下的超速。(8)该控制策略能有效地限制瞬态期间IHX空间温度分布的时间变化。从本质上讲,IHX的行为方式可以使IHX的每个点在瞬态过程中经历大约相同的温度变化率。(9)发现闭环布雷顿循环的稳定性对汽机性能图上的操作位置很敏感。这里存在着相互竞争的利益:更稳定的运行意味着在降低整体循环效率的曲线上运行。今后的工作应更详细地处理在这项工作过程中暴露出来的因素。具体而言:(1)在使用反应器出口温度控制器时,应进行稳定性分析,以识别控制反应器出口温度稳定性的现象。目标是确定一个性能更好的控制器。(2)未来的模拟应采用多轴节点。本工作中使用的堆芯单轴节点模型会产生初始堆芯反应堆出口温度扰动,这是一个数值伪影。(3)上述关于Brayton循环稳定性和效率对性能曲线特征和使用的依赖的权衡需要更好地理解。(4)氙气的作用在本工作中被忽视,需要在今后的工作中纳入。
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Heat exchanger temperature response for duty-cycle transients in the NGNP/HTE.
Control system studies were performed for the Next Generation Nuclear Plant (NGNP) interfaced to the High Temperature Electrolysis (HTE) plant. Temperature change and associated thermal stresses are important factors in determining plant lifetime. In the NGNP the design objective of a 40 year lifetime for the Intermediate Heat Exchanger (IHX) in particular is seen as a challenge. A control system was designed to minimize temperature changes in the IHX and more generally at all high-temperature locations in the plant for duty-cycle transients. In the NGNP this includes structures at the reactor outlet and at the inlet to the turbine. This problem was approached by identifying those high-level factors that determine temperature rates of change. First are the set of duty cycle transients over which the control engineer has little control but which none-the-less must be addressed. Second is the partitioning of the temperature response into a quasi-static component and a transient component. These two components are largely independent of each other and when addressed as such greater understanding of temperature change mechanisms and how to deal with them is achieved. Third is the manner in which energy and mass flow rates are managed. Generally one aims for a temperature distribution that minimizes spatial non-uniformity of thermal expansion in a component with time. This is can be achieved by maintaining a fixed spatial temperature distribution in a component during transients. A general rule of thumb for heat exchangers is to maintain flow rate proportional to thermal power. Additionally the product of instantaneous flow rate and heat capacity should be maintained the same on both sides of the heat exchanger. Fourth inherent mechanisms for stable behavior should not be compromised by active controllers that can introduce new feedback paths and potentially create under-damped response. Applications of these principles to the development of a plant control strategy for the reference NGNP/HTE plant can be found in the body of this report. The outcome is an integrated plant/control system design. The following conclusions are drawn from the analysis: (1) The plant load schedule can be managed to maintain near-constant hot side temperatures over the load range in both the nuclear and chemical plant. (2) The reactor open-loop response is inherently stable resulting mainly from a large Doppler temperature coefficient compared to the other reactivity temperature feedbacks. (3) The typical controller used to manage reactor power production to maintain reactor outlet temperature at a setpoint introduces a feedback path that tends to destabilize reactor power production in the NGNP. (4) A primary loop flow controller that forces primary flow to track PCU flow rate is effective in minimizing spatial temperature differentials within the IHX. (5) Inventory control in both the primary and PCU system during ramp load change transients is an effective means of maintaining high NGNP thermal efficiency while at reduced electric load. (6) Turbine bypass control is an effective means for responding to step changes in generator load when equipment capacity limitations prevent inventory control from being effective. (7) Turbine bypass control is effective in limiting PCU shaft over speed for the loss of generator load upset event. (8) The proposed control strategy is effective in limiting time variation of the differential spatial temperature distribution in the IHX during transients. Essentially the IHX can be made to behave in a manner where each point in the IHX experiences approximately the same temperature rate of change during a transient. (9) The stability of the closed-loop Brayton cycle was found to be sensitive to where one operates on the turbo-machine performance maps. There are competing interests: more stable operation means operating on the curves at points that reduce overall cycle efficiency. Future work should address in greater detail elements that came to light in the course of this work. Specifically: (1) A stability analysis should be performed to identify the phenomena that control reactor outlet temperature stability when operating with the Reactor Outlet Temperature Controller. The goal is to identify a better performing controller. (2) Future simulations should be performed with multiple axial nodes. The single axial node model for the core used in this work gives rise to an initial core reactor outlet temperature perturbation that is a numerical artifact. (3) The tradeoffs referred to above regarding the dependence of Brayton cycle stability and efficiency on performance curve characteristics and use need to be better understood. (4) The role of xenon was neglected in this work and needs to be included in future work.
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