An Operation Scheme Generation Method for Nuclear Power Plant Operation under the Condition of No Operating Procedures Guided

Abstract

Large-scale, complex, and high-risk industrial systems such as nuclear power plants have developed detailed operating procedures. Under the expected conditions, the operators operate the system according to the operating procedures to avoid human error. However, under complex and unfamiliar conditions, once the guidance of operating procedures is lost, serious consequences may be caused. This paper proposes a No-Procedure guided Operation Supervision Technology (NoP-OST). The key idea is to identify the success paths by a forward-searching approach from source to sink functions. On this basis, the success paths are combined to generate various operation schemes to achieve the main objectives of the system. The paper illustrates the application of NoP-OST through the case of loss of the Residual Heat Removal System (RHRS) in a Pressurized Water Reactor (PWR) nuclear power plant. The research results show that the method proposed in this paper can provide a valuable operational reference for complex systems by making use of the available functions of the system.

1. Introduction

Ensuring safety is the unswerving goal throughout the life cycle of nuclear power plants (NPPs), including design, construction, operation, maintenance, and decommissioning. Hardware failures and human errors constitute the main causes of operation events and accidents at NPPs. Among them, the incidents and accidents in the early NPPs are mainly attributed to hardware failure. After the introduction of new materials and technologies to improve the durability and reliability of equipment [1], the probability of hardware failure in NPPs has been significantly reduced, and human error has risen to be the causative factor in incidents and accidents at NPPs. According to the statistics of the NNSA (China National Nuclear Safety Administration) for 14 years [2,3,4,5,6,7,8,9,10,11,12,13,14,15], incidents caused by human error accounted for 51% and even reached 73.9% in 2016.

After the Three Mile Island (TMI) accident, the nuclear industry has been committed to reducing the load and human error of operators by various means, such as improving the automation level of NPPs, improving human-machine interfaces (HMI) and operating procedures, developing operator support systems (OSS), enhancing operator training, etc. [16]. After these efforts, the number of human errors caused by operators in normal operations has decreased year by year. However, the prevention of human error in unfamiliar conditions is still one of the types of research focuses [17]. One of the lessons learned from three serious nuclear accidents (namely, the Three Mile Island nuclear accident, the Chornobyl nuclear accident, and the Fukushima nuclear accident) is that the probability of operator human errors in completely unfamiliar environments will significantly increase [18]. According to the statistics of the incidents in the first seven years of operation of six new NPPs in China (as shown in Figure 1), it is found that although the total number of incidents has fluctuated in the first four years, the proportion of human error has increased year by year. In the following three years, the proportion of human error and the number of incidents showed a slow downward trend. This trend change is related to the operator’s unfamiliarity with the NPPs, unskilled operation, and the running-in with the NPPs at the initial stage of plant operation. Therefore, it is necessary and urgent to strengthen the supervision of operators in unfamiliar plant operating conditions.

Figure 1. Statistics of incidents in the first seven years of China’s new NPPs.

NPPs generally conduct team cooperation through shift supervisor supervision and cross-validation among operators to reduce human error [19]. However, the members of the same operation team may have great relevance in terms of knowledge, skills, working environment, perception and decision-making ability, and fatigue degree. The performance of supervisors and operators may deteriorate at the same time, which will weaken the effect of operation supervision [20]. In recent years, the energy industry has begun to introduce various computer intelligent decision-making methods to improve the safety [21,22,23,24]. Computer intelligent supervision technology can make use of the advantages of massive memory, fast calculation, and never fatigue to make up for the deficiencies of operators and prevent human error.

In the previous study, the author proposed the Operating Procedures Supervision System (OPSS) to implement operator supervision under the guidance of operating procedures [25]. Operating procedures are a group of actions with a time sequence, according to which the NPP operators can establish or maintain the functions of systems and equipment to achieve specific operational objectives. Each operating procedure is not the only means to achieve an operational objective, but an operation strategy that has been verified and proved to be safe, reliable, easy to implement, and can achieve the operation objective under an expected condition. However, under some special conditions, the operators may be in a situation where there is no operating procedure available, or all operating procedures are not fully applicable. In the absence of operating procedure guidance, the probability of operator error will increase. After the Fukushima nuclear accident, the Nuclear Energy Institute (NEI) put forward the FLEX strategy (Diverse and Flexible Coping Strategies) [26], which aims to establish the ability to prevent fuel and spent fuel from damage and maintain the containment function for a long time by using fixed equipment, on-site mobile equipment and preset off-site resources.

Operators utilize various knowledge to identify available systems, equipment, and functions to achieve operational objectives in unfamiliar NPP operation conditions, and therefore bear the high cognitive load and are prone to human error. This paper proposes a No-Procedure guided Operation Supervision Technology (NoP-OST) based on the system function model to help operators understand the system operation objectives, available functions, and equipment, automatically identify the reference path to achieve the operational objectives and achieve the purpose of reducing human error.

The following chapters are arranged as follows: Section 2 presents the method of the NoP-OST; a case is given in Section 3 to illustrate the use of the NoP-OST; the characteristics of the NoP-OST are discussed and summarized in the last chapter.

2. Design of NoP-OST

2.1. Overall Design

Figure 2 shows the functional block diagram of the overall design of NoP-OST. The NoP-OST starts with plant operation monitoring which monitors the performance of the critical systems and equipment and analyzes whether the plant operation deviates from the objectives to be achieved. If there is no deviation, it means that the current operating procedures are still applicable, and the current operation strategy is to implement and monitor the established operation procedures. If the current plant operation deviates from the operation objectives, the established operating procedures may not be applicable, and the new operation objective of the plant needs to be identified. Once the new operation objectives are determined, the next step is to analyze the available functions to identify which plant functions are still effective and can be used to achieve the operational objectives. It is worth noting that the available functions include those defined in the plant design, such as engineered safety features (ESF), as well as the potential capabilities of systems and equipment. These potential capabilities are inherent in the systems and equipment. Although they are not clearly defined in the design of an NPP, they can be utilized to play a substitute role for designed functions under special operating conditions. Under specific conditions, the available functions of the plant can be organized to form one or more success paths to achieve the operational objectives. It should also be noted that operating procedures are only part of these success paths. The difference between operating procedures and other success paths is that operating procedures are usually success paths that have been verified and validated to be reliable and easy to implement. If there are available operating procedures under the current operation objectives, it should be the first choice to implement the operating procedures and monitor the implementation of the operating procedures. In this case, the achievement of the operating objectives is credible.

Figure 2. Functional block diagram of NoP-OST.

In the absence of available operating procedures, the identified success paths can be used as a reference for formulating various operation schemes. The implementation of the operation scheme is to take specific control actions to operate the systems and equipment to establish one or several successful paths, and finally achieve the operation objectives.

2.2. Success Path Identification Method

How to identify the success paths by utilizing the available functions to achieve the operational objectives is a key issue of NoP-OST. This paper adopts a Flow-based functional modeling approach [27] to describe the relationship between available functions and operational objectives. Flow-based approaches model a system by focusing on the flows (of mass, energy, or information) in the system and on the component actions on the considered flows [28]. In the NoP-OST, Multilevel Flow Modeling (MFM) is selected to build various system models of NPP. As shown in Figure 3, MFM provides common basic functions, such as source, sink, transport, barrier, storage, and balance, for representing mass, energy, and information [29]. Instances of these functions are connected to build function structures (i.e., flow structures). Functions can be linked to objectives (i.e., purposes of the system) by means-ends relations, representing that a set of functions are used to achieve the objectives. An objective can be also linked to functions, representing that the objective must be fulfilled for the functions to be available. The latest development of MFM provides control functions [30]. MFM has been usually applied as a cause-consequence reasoning technique for the purposes of fault diagnosis or alarm analysis of process systems including NPP, where the means-ends analysis strategy is commonly used. Starting from the objectives and through a top-down and backward-searching approach, the causal paths that endanger the achievement of the objectives in an MFM model are identified [31,32,33,34]. The application of MFM also serves for hazard analysis, which adopts a forward analysis method. The impact of an abnormal function on the objectives is analyzed and reasoned by utilizing a bottom-up and forward reasoning approach [35]. Yang [36] presents a method of utilizing MFM for quantitative reliability analysis. Song [37] proposed an MFM-based operation search method for planning the operation of complex process units. Recently, a model and rule-based operational process synthesis (OPS) system is proposed from the perspective of functional state transition [38].

Figure 3. Elements of MFM.

Each MFM element of MFM represents a category of process phenomenon that can be mathematically represented. The mathematical expressions of some MFM functions which will be used later in this article are provided by Formulas (1)–(4), corresponding to the storage, balance, transport, and barrier functions, respectively. Further information on the mathematical basis of MFM elements can be found in reference [29]:

$$\frac{\mathrm{dv}}{\mathrm{dt}}={\displaystyle \sum }{\mathrm{F}}_{\mathrm{i}}-{\displaystyle \sum }{\mathrm{F}}_{\mathrm{o}}$$

(1)

$${\displaystyle \sum }{\mathrm{F}}_{\mathrm{i}}={\displaystyle \sum }{\mathrm{F}}_{\mathrm{o}}$$

(2)

$${\mathrm{F}}_{\mathrm{i}}={\mathrm{F}}_{\mathrm{o}}$$

(3)

$${\mathrm{F}}_{\mathrm{o}}=0$$

(4)

where ${\mathrm{F}}_{\mathrm{i}} ,{ \mathrm{F}}_{\mathrm{o}} ,$ and $\mathrm{v}$ represents the input, output, and accumulated quantity of a physical component, respectively.

The principle of success path identification based on MFM models is illustrated in Figure 4. The model shown in Figure 4 is a hypothetical MFM model that is not specific to specific objects. In this model, the system objective (obj) is realized by a flow structure composed of two sources (sou1 and sou2), two sinks (sin1 and sin2), and four transport functions (tra1, tra2, tra3, and tra4). It is further assumed that the objective obj is achieved by either sub-objective obj1 or obj2 which are directly implemented by the functions tra3 and tra4, respectively.

Figure 4. Principle of success path identification using MFM.

The available functions shall be identified before the successful path identification. The available function identification proceeds downwards from the objective obj, via the means-ends relation, into the connected flow network of functions, each of which is investigated (by sensor reading or on-site measurement) to find out whether it is available or not. In this example, it is assumed that the tra3 function is not available.

The success path identification starts from each source function and is analyzed forward along the flow direction. If the current path (the smallest one consists of one source function) has an available downstream function (except for storage and balance functions), the current path and downstream functions are connected to form a new path. Repeat this process repeatedly until the path reaches a sink function, thus forming a complete path from the source function to the sink function. If the downstream function of the current path is a storage or balance function (these two types of MFM functions can have multiple outputs), connect the storage or balance function to the current path, and copy the new path according to the output number of the storage or balance function, so that each new path corresponds to the output of the storage or balance function. Figure 5 shows the four complete paths of the MFM model shown in Figure 4 identified by this method. Among them, both path 1 and path 3 contain the unavailable tra3. Therefore, these two paths are not success paths unless tra3 can be recovered, and paths 2 and 4 are success paths.

Figure 5. Identified success paths.

3. Case Study

The Residual Heat Removal System (RHRS) is the main cooling means for Pressurized Water Reactor (PWR) nuclear power plant during the shutdown. This paper describes the NoP-OST with the loss of cooling of the RHRS incident of a PWR after reactor shutdown as an example. Figure 6 shows the structure of the RHRS (marked with the red line in the figure) and other related reactor cooling functions. The description of the relevant equipment in Figure 6 is given in Table 1. The main functions of the RHRS are as follows:

(1)

When the secondary loop is out of service, the RHRS removes the shutdown residual heat of the core and the sensible heat of the primary, loop coolant, and equipment.

(2)

When the reactor is in the shutdown state for loading, unloading, or maintenance, the RHRS removes the residual heat of the core and maintains the primary loop at a low temperature.

(3)

During the reactor start-up, the RHRS ensures the circulation of the primary loop coolant.

Figure 6. The structure of RHRS and the associated system of a PWR. The red part in the Figure 6 represents the failed of RHR system.

Table 1. Description of the equipment in Figure 6.

No.	Equipment	Explanation
1	SG	Steam generator
2	RCP	Reactor coolant pump
3	RCP212VP	Primary loop motor-driven valve
4	RRA001VP	RHRS motor-driven valve
5	RRA001PO	RHRS pump
6	RRA014VP	RHRS motor-driven valve
7	VB	Steam bypass isolation valve
8	RWST	Refueling water storage tank (RWST)
9	005FI	Floor sump filter
10	006FI	Floor sump filter
11	014VB	Floor sump manual isolation valve
12	RIS051VP	Safety Injection System (SIS) motor-driven valve
13	RIS001VB	SIS isolation valve
14	RIS075VB	SIS isolation valve
15	RIS001PO	Low-pressure safety injection pump
16	063VP	Primary loop motor-driven valve
17	RCV001PO	High-pressure safety injection pump
18	021VP	Primary loop motor-driven valve
19	032VP	Safety Injection Tank (SIT) motor-driven valve

Table 1. Description of the equipment in Figure 6.

No.	Equipment	Explanation
1	SG	Steam generator
2	RCP	Reactor coolant pump
3	RCP212VP	Primary loop motor-driven valve
4	RRA001VP	RHRS motor-driven valve
5	RRA001PO	RHRS pump
6	RRA014VP	RHRS motor-driven valve
7	VB	Steam bypass isolation valve
8	RWST	Refueling water storage tank (RWST)
9	005FI	Floor sump filter
10	006FI	Floor sump filter
11	014VB	Floor sump manual isolation valve
12	RIS051VP	Safety Injection System (SIS) motor-driven valve
13	RIS001VB	SIS isolation valve
14	RIS075VB	SIS isolation valve
15	RIS001PO	Low-pressure safety injection pump
16	063VP	Primary loop motor-driven valve
17	RCV001PO	High-pressure safety injection pump
18	021VP	Primary loop motor-driven valve
19	032VP	Safety Injection Tank (SIT) motor-driven valve

3.1. Objective Identification

During the reactor shutdown, the core residual heat is mainly discharged by the RHRS to maintain the primary loop temperature. This paper selects the most extreme case, that is, the complete failure of the RHRS, to explain the application of the NoP-OST.

The RHRS failure indicates the core has lost cooling. In this case, the main objective of NPP is “to maintain the cooling capacity” to lower the primary loop temperature.

In addition to the RHRS, the additional core cooling function can be provided by Safety Injection System (SIS) and the secondary loop.

The SIS provides the following three sources of coolant:

(1)

Safety Injection Tank (SIT).

(2)

Refueling water storage tank (RWST).

(3)

Floor sump.

The SIS injects water into the primary pool to cool the reactor in the following three ways:

(1)

Pressure of SIT: the SIT is filled with high-pressure helium. When necessary, the coolant in SIT can be pumped into the primary loop according to the pressure difference between SIT and the primary loop.

(2)

High-pressure safety injection pump (RCV001PO): the coolant in the RWST is pumped into the primary loop through forced circulation.

(2)

Low-pressure safety injection pump (RIS001PO): the coolant in the floor sump and RWST is pumped into the primary loop through forced circulation.

3.2. MFM of Maintaining Reactor Core Cooling

According to the selected operation objective (i.e., maintaining reactor core cooling), the MFM model is given, as shown in Figure 7.

Figure 7. MFM model of maintaining reactor core cooling.

The red part in the Figure 7 represents the failed of RHR system.

Table 2 shows the explanation of each main model element. The MFM model consists of four flow structures.

(1)

Efs1: is an energy flow for maintaining core cooling by removing the heat generated by the reactor (to achieve the objective obj0).

(2)

Mfs1: is a mass flow for providing enough coolant in the primary loop (to achieve the objective obj1).

(3)

Mfs2: is a mass flow for providing enough feedwater in the secondary loop (to achieve the objective obj2).

(4)

Mfs3: is a mass flow for driving the coolant flow in the RHRS (to achieve the objective obj3). Since the RHRS is assumed to fail, this mass flow is simplified to a higher degree.

Table 2. The explanation of the main MFM elements in Figure 7.

ID	Function Description	Notes
Obj0	Maintain reactor core cooling	Main objective
Obj1	Maintain primary coolant flow	By the primary loop and supporting facilities
Obj2	Maintain secondary coolant flow	By the secondary loop
Obj3	Coolant supply from the RHRS	By the RHRS
So1	Reactor core heat generation
So2	Primary coolant supply
So3	Coolant supply for high-pressure SIS	By the SIT
So4	Coolant supply for high-pressure or low-pressure SIS	By the RWST
So5	Coolant supply for reactor long-term cooling	By the floor sump
So6	Coolant supply for the secondary loop
So7	Coolant supply for the RHRS	By the primary loop
Si1	Heat consumption through turbine work
Si2	Heat consumption in the condenser
Si3	Heat consumption in the floor sump
Si4	Heat consumption in the RHRS
Si5	Primary coolant flows back to the cold-leg pipe section
Si6	Primary coolant flows into the floor sump
Si7	Secondary coolant flows into the condenser
Si8	Coolant injects into the primary loop
Tr1	Heat transfer from fuel to the primary loop
Tr2	Heat transfer from the primary loop to the SG	By the RCP
Tr3	Heat transfer from the SG to the turbine
Tr4	Heat transfer from the SG to the condenser	Via the VB
Tr5	Heat transfer from the primary loop to the RHRS
Tr6	Primary coolant flows to the reactor vessel
Tr7	Coolant flows to the reactor vessel	Via high-pressure SIS
Tr8	Coolant flows to the reactor vessel	Via low-pressure SIS
Tr9	Coolant flows to the reactor vessel	Via circulating cooling pipelines
Tr10	Primary coolant flows to the SG
Tr11	Primary coolant flows to the cold-leg pipe section	By the RCP
Tr12	Secondary coolant flows to the SG
Tr13	Secondary coolant flows to the turbine
Tr14	Secondary coolant flows to the condenser	From the VB
Tr15	Secondary coolant flows to the condenser	From the turbine
Tr16	Secondary coolant flows to the condenser	From the turbine or SG
Tr17	Coolant flows to the primary loop	By the RHRS
St1	Heat storage in the primary loop	By primary coolant system
St2	Heat storage in the SG	By steam generator
St3	Coolant storage in the reactor vessel	By reactor vessel
St4	Coolant storage in the SG	By steam generator (secondary side)
Bl1	Coolant flows in the SG	Primary loop side
Bl2	Flow connection between Tr13 and Tr15	By pipeline
Bl3	Flow connection between Tr14 and Tr15	By pipeline
Bar1	Prevent the primary loop from injecting the heat into the floor sump	By the discharge valve
Bar2	Prevent the primary loop from injecting coolant into the floor sump	By the discharge valve

Table 2. The explanation of the main MFM elements in Figure 7.

ID	Function Description	Notes
Obj0	Maintain reactor core cooling	Main objective
Obj1	Maintain primary coolant flow	By the primary loop and supporting facilities
Obj2	Maintain secondary coolant flow	By the secondary loop
Obj3	Coolant supply from the RHRS	By the RHRS
So1	Reactor core heat generation
So2	Primary coolant supply
So3	Coolant supply for high-pressure SIS	By the SIT
So4	Coolant supply for high-pressure or low-pressure SIS	By the RWST
So5	Coolant supply for reactor long-term cooling	By the floor sump
So6	Coolant supply for the secondary loop
So7	Coolant supply for the RHRS	By the primary loop
Si1	Heat consumption through turbine work
Si2	Heat consumption in the condenser
Si3	Heat consumption in the floor sump
Si4	Heat consumption in the RHRS
Si5	Primary coolant flows back to the cold-leg pipe section
Si6	Primary coolant flows into the floor sump
Si7	Secondary coolant flows into the condenser
Si8	Coolant injects into the primary loop
Tr1	Heat transfer from fuel to the primary loop
Tr2	Heat transfer from the primary loop to the SG	By the RCP
Tr3	Heat transfer from the SG to the turbine
Tr4	Heat transfer from the SG to the condenser	Via the VB
Tr5	Heat transfer from the primary loop to the RHRS
Tr6	Primary coolant flows to the reactor vessel
Tr7	Coolant flows to the reactor vessel	Via high-pressure SIS
Tr8	Coolant flows to the reactor vessel	Via low-pressure SIS
Tr9	Coolant flows to the reactor vessel	Via circulating cooling pipelines
Tr10	Primary coolant flows to the SG
Tr11	Primary coolant flows to the cold-leg pipe section	By the RCP
Tr12	Secondary coolant flows to the SG
Tr13	Secondary coolant flows to the turbine
Tr14	Secondary coolant flows to the condenser	From the VB
Tr15	Secondary coolant flows to the condenser	From the turbine
Tr16	Secondary coolant flows to the condenser	From the turbine or SG
Tr17	Coolant flows to the primary loop	By the RHRS
St1	Heat storage in the primary loop	By primary coolant system
St2	Heat storage in the SG	By steam generator
St3	Coolant storage in the reactor vessel	By reactor vessel
St4	Coolant storage in the SG	By steam generator (secondary side)
Bl1	Coolant flows in the SG	Primary loop side
Bl2	Flow connection between Tr13 and Tr15	By pipeline
Bl3	Flow connection between Tr14 and Tr15	By pipeline
Bar1	Prevent the primary loop from injecting the heat into the floor sump	By the discharge valve
Bar2	Prevent the primary loop from injecting coolant into the floor sump	By the discharge valve

3.3. Success Path Identification

By using the method proposed in Section 2.2, the MFM model shown in Figure 7 is analyzed, and the successful paths are shown in Figure 8. As shown in Figure 8, the energy flow Efs1 contains 4 paths, and the mass flow Mfs1, Mfs2, and Mfs3 contain paths 8, 2, and 1, respectively. The physical meaning of each path is shown in Table 3. According to the assumption, the path corresponding to Mfs3 is unavailable, which also leads to the unavailability of Tr5 and path 4 in the Efs1 (which contains the unavailable Tr5).

Figure 8. Paths identified from the MFM model in Figure 7.

Table 3. Explanation of each identified path.

Flow Structure	Path	Explanation
Efs1	1	The heat generated by the reactor is transferred to the steam turbine for work
	2	The heat generated by the reactor is transferred to the condenser
	3	The heat generated by the reactor is exported to the floor sump
	4	The heat generated by the reactor is exported to the RHRS (Unavailable by the consequence of the failure of RHRS)
Mfs1	1	Coolant flows in the primary loop
	2	Coolant flows from the SIT to the floor sump
	3	Coolant flows from the RWST to the floor sump
	4	Long-term coolant circulation that takes coolant from the floor sump and flows back to the floor sump through the primary loop
	5	Coolant flows into the floor sump from the primary loop. In the absence of an external water source, the primary loop coolant will become insufficient.
	6	Coolant flows from the SIT into the primary loop. In case of no coolant discharge, the primary loop pressure will continue to rise.
	7	Coolant flows from the RWST into the primary loop. In case of no coolant discharge, the primary loop pressure will continue to rise.
	8	Coolant flows from the floor sump into the primary loop. In case of no coolant discharge, the primary loop pressure will continue to rise.
Mfs2	1	Secondary coolant circulates in the secondary circuit through the turbine.
	2	Secondary coolant circulates in the secondary circuit through the VB.
Mfs3	1	Coolant flows in the RHRS. (Unavailable by the assumption)

Notes: A path with a red background indicates that the path is currently unavailable. A path with yellow background indicates that the path has obvious hazardous consequences.

Among the eight paths contained in Mfs1, paths 5–8 have obvious hazard consequences. If these hazard consequences cannot be dealt with well, the corresponding paths cannot be considered engineering solutions.

The path in the red boxes is not available, the path in the yellow boxes have hidden danger.

Based on the above analysis, six success paths are finally identified from the MFM model shown in Figure 7, which are summarized in Table 4. The success paths 1-1 and 2-1 need to establish the primary and secondary mass flow, that is, these two success paths contain one energy flow and two mass flows respectively. Other success paths only include one energy flow and one mass flow. The success path 4-1 is assumed to be a failure in this paper. If the failure can be corrected, then the path is available. Figure 9 shows the flows of mass and energy required for various success paths.

Table 4. Success paths identified after removing the paths with obvious hazard consequences.

Energy Paths		Mass Paths		Success Paths
1		Mfs1-path1		Path 1-1: Restart the primary and secondary loops to exhaust the heat through the turbine work
		Mfs2-path1
2		Mfs1-path1		Path 2-1: Restart the primary and secondary loops to discharge the heat directly into the condenser through the steam bypass pipeline
		Mfs2-path2
3		Mfs1-path2		Path 3-1: Start the high-pressure SIS and discharge the heat into the floor sump through the discharge valve
		Mfs1-path3		Path 3-2: Start the low-pressure SIS and discharge the heat into the floor sump through the discharge valve
		Mfs1-path4		Path 3-3: Start the circulating cooling and discharge the heat into the floor sump through the discharge valve
4		Mfs3-path1		Path 4-1: Export heat through the RHRS

Figure 9. The required mass and energy flows corresponding to each success path.

3.4. Operation Scheme Analysis

The success path 1-1 can well meet the demand for reactor core cooling and generate additional power supply. However, it should be noted that when the temperature of the primary loop becomes too low, the unsaturated steam generated in the SG may damage the turbine blades and reduce the life of the turbine. The success path 2-1 can well meet the cooling demand without additional negative effects. In the success paths 3-1, SIT stores low-temperature coolant. However, due to its limited volume, it is difficult for the SIT to provide cooling for a long time. As for the success path 3-2, although the RWST stores a considerable amount of coolant, it is still difficult to provide cooling for a long time. The success path 3.3 establishes a coolant circulation between the primary loop and the floor sump. The heat exchanger can be used for long-term cooling with the environment, so it can be used for long-term reactor core cooling. However, paths 3-1, 3-2 and 3-3 should not be selected unless necessary, because they may cause overpressure in the primary loop and damage the integrity of the primary loop.

Therefore, based on the advantages and disadvantages of the above success paths, it is suggested that the priority of the implementation of the operation plan should be the success path 2-1, path 1-1, path 3-3, path 3-2, and path 3-1.

4. Discussion and Conclusions

Nuclear power plants usually develop operating procedures for various working conditions, and operators can skillfully implement the procedures to avoid human errors. The Three Mile Island and Fukushima nuclear accidents have revealed that serious consequences will occur if operators have no operating procedure guidance under unfamiliar conditions. In this context, some international organizations, including the IAEA and the NEA, have proposed evaluating the defense in depth of NPPs and enhancing their ability to respond to severe accidents [39,40].

This paper proposes a No-Procedure guided Operation Supervision Technology (NoP-OST) which can be used to assist operators to establish various reasonable operation schemes under unfamiliar operating conditions of NPPs. A success path identification method is proposed. This paper selects MFM as the system modeling approach because this method can well meet the characteristics of NPPs in achieving safety and economic objectives by establishing various mass, energy, and information flows. The success paths are identified according to the structure of a set of functional MFM models which reflect the dependency between objectives and functions of specific plant systems. MFM models the system at different levels of means-ends, which is conducive to simplifying the identification of success paths to achieve the system objectives.

The success path identification by MFM commonly employs a means-end analysis approach which involves a top-down and backward searching from the objectives of MFM models. This strategy assumes that the MFM models have already well-established the correlation between system objectives and functions through task analysis.

In this paper, the search for success paths starts from a source function and proceeds with forward searching until a sink function is reached. This is because NPPs always achieve their operational objectives by providing material, energy, and information channels. This strategy cannot guarantee that the identified success paths will necessarily achieve the system’s objectives but can maximize the identification of success paths within the model’s scope. This is because the paper assumes that some success paths that were considered impossible or difficult to implement in the design phase may have been ignored during MFM modeling. However, under specific operating conditions, these paths can provide a technical means to ensure nuclear safety. As shown in the case study, the original purpose of the safety injection system was to supplement the coolant in the primary loop. However, through analysis, it was found that the injection system, along with the use of the discharge valve, can provide a certain cooling capacity. Therefore, a key point of the proposed method is that it is necessary to carry out operation scheme analysis by plant personnel to form various alternatives to achieve the main objectives by combining various success paths. As the case study shows, some success paths have preconditions or harmful consequences for implementation, which have not yet been reflected in the MFM model, and additional information needs to be supplemented by engineering experience or other methods such as by a full-scale simulator of the NPP. In other words, the proposed NoP-OST is currently a semi-automated framework that requires combining domain knowledge with automatic success path identification to form applicable operation schemes.