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Modeling of Electrodialysis Plant at Water Treatment Facility Using Fuzzy Cognitive Map Theory

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24 July 2025

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28 July 2025

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Abstract
Water is a fundamental resource for sustainable demographic, social, and economic development. Today, water scarcity is a major challenge due to population growth, industrial expansion, pollution from human activities, and the limited availability of freshwater resources. Therefore, advanced water purification and treatment methods—such as reverse osmosis, chemical precipitation, adsorption, membrane processes, ion exchange, photocatalysis, chemical oxidation and reduction, electrodialysis, and ultrafiltration—are being actively developed to treat wastewater before discharge into the environment. In our study, we propose to use fuzzy cognitive maps (FCM) to analyze the operating factors of an electrodialysis water purification facility. FCM is appropriate for this system due to its complexity and the limited feasibility of conducting numerous experiments to determine direct dependencies. The initial mathematical model based on FCM was constructed using expert knowledge of the electrodialysis water purification process. The initial FCM was then refined using a learning algorithm, enabling the discovery of hidden relationships within the system. The proposed model enables identification of the optimal equipment configuration for operating a water treatment facility to maintain water resource balance.
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1. Introduction

Simulation is a valuable tool for evaluating the effective parameters in various processes, especially in water treatment. In fact, it not only enhances understanding of the process but also enables simulation with minimal experimental data.
In recent years, increased computing power and the availability of graphics processors have enabled more complex hydrodynamic models that replicate natural processes using input data. The ability to model processes occurring during electrodialysis opens up opportunities for the practical use of the phenomenon of electroconvection, which is an important step towards a much wider application of electrodialysis on an industrial scale.
Electrodialysis (ED) is an economically and environmentally efficient method for desalination, concentration and separation of natural and industrial solutions. The broader application of this method is hindered by certain limitations encountered in traditional use. These include a low mass transfer rate due to diffusion limitations, membrane surface fouling, and unwanted generation of H⁺ and OH⁻ ions at the membrane/solution interface. Applying high current densities or voltages in ED has been shown to overcome some of these limitations. Based on direct numerical modeling of the Nernst-Planck-Poisson and Navier-Stokes equations, a group of scientists [1,2] constructed several 1D-2D-3D mathematical models to describe the transfer of salt ions in a desalination channel under overlimit current conditions. A group of scientists [3] also created a 2D model describing the combined contribution of spacers, electroconvection, and water dissociation/recombination reactions. It is used to determine the fundamental patterns of interaction between spacer geometry and current density and their influence on the transfer processes and solution flow. The overlimit current mode is economically advantageous for desalination of dilute solutions, since electroconvective vortices developing in this mode allow a significant increase in the rate of useful mass transfer, which saves the area of expensive membranes [4]. The broader adoption of the overlimit current mode is hindered by limited understanding of the complex physicochemical processes it involves.
The complex relationships between the input and output parameters of the electrodialysis plant setup can be solved by nonlinear methods known as computational intelligence methods [5]. The most reliable and powerful computational intelligence methods include data-driven systems such as neural networks, genetic algorithms and fuzzy logic models, which have attracted much attention as effective methods for environmental applications. In recent years, water treatment process prediction has been carried out using various models such as artificial neural networks (ANN) [6,7], adaptive neuro-fuzzy inference system [8], least-squares support vector machines [9], random forest [10], response surface methodology [11], genetic algorithm [12] and fuzzy inference system [13].
Due to the need to include not only quantitative but also qualitative parameters in the model, fuzzy models have recently become widespread, including the FCM approach described by Kosko [14]. It has the ability to convey expert experience in the form of indices that can be calculated using uncertain, vague and subjective information. In essence, the fuzzy inference system produces evaluation results in the form of linguistic terms that are understandable to managers, decision makers and non-experts [15]. There are a small number of published studies that have used the fuzzy logic approach to model the performance of an electrodialysis plant [16]. Guolin Jing et al. [17] applied a fuzzy logic model to predict the percentage of NaCl solution separation depending on voltage and flow rate. Hanife Sari et al. [18] developed an FCC model to simulate a new integrated process (UF-IER-EDBM-FO) consisting of ultrafiltration (UF), ion exchange resins (IER), bipolar membrane electrodialysis (EDBM) and Fenton oxidation units (FO). Kyriakarakos et al. [19,20] developed a variable load energy management system (EMS) based on FCM.
These studies confirm the possibility of applying fuzzy logic techniques to water purification problems, in particular, to predict electrodialysis in a membrane system. However, in the known models, the list of parameters used is limited and does not include high-level system parameters such as price or membrane service life, which are included in this work.

2. Materials and Methods

This section describes the general methods used in FCM theory, which are used to construct the model structure and predict the evolution of the system after changing the values of the model components. A brief introduction to FCM theory and the basic equation used for scenario modeling is provided.
FCM is a soft computing method that can be used to describe, analyze, and model complex systems. Originally introduced by Kosko [14], FCM takes the form of a knowledge graph consisting of nodes representing concepts and links between them. Concepts are nonlinear and represent variables in a causal system, with their states taking values within a specified range A i t [ 0 , 1 ] . Links in an FCM model reflect the presence and strength of causal links between concepts. The strength of a link is determined by the weight of an arc of a directed graph and takes a value in the range w j i [ 0 , 1 ] if negative causal links are not taken into account in the model, or w j i [ 1 , 1 ] if negative causal links are taken into account.
The list of concepts, connections and connection weights are determined based on expert knowledge, research data, statistical properties of the system or historical data about the system. Such a fuzzy model describes the state of the system at a certain point in time in M -dimensional space, where M is the number of concepts in the system.
Figure 1 shows a simple FCM with five concepts and ten weighted relationships. FCMs are weighted directed graphs that can model the relationships or causality that exist among the features of a system. The concepts are represented by nodes С 1 , С 2 , С 3 , С 4 and С 5 .
The connection is always directed from the concept of cause to the concept of effect. For example, in Figure 1, with С 1 С 2 , when is said С 1 have an effect on C 2 , that is, С 1 is a causal concept, while C 2 is a concept of effect. If the connection is positive, then the concept С 1 has a positive effect on the concept C 2 , otherwise negative. Each concept is characterized by a number A i , which represents its value, and is the result of mapping the real value of the system variable into the interval [ 0 , 1 ] .
The model underlying the standard FCM can be characterized by a set of 4 components C ,   W ,   A ,   f , where C   =   C 1 , C 2 , .. C m is a set of concepts of dimension m , constructed on the basis of fuzzy sets, W :   C × C 1 , 1 is a matrix of influence weights w i j 1 , 1 , assigned to each pair of concepts C i   ,   C j dimension n × n . The value w i j determines the sign and weight of the arc connecting the causal concept C i and the concept of the effect C j . The function A :   C A i t determines the magnitude of the activation A i t R t of each concept C i at a discrete moment in time t = 1 ,   2 ,   ... , t f i n a l . The activation function f :   R   I aggregates the magnitude of the impact of causal concepts on the target concept and limits the result within the interval [ 0 , 1 ] . The interpretation of the causal relationship w i j between two concepts, C i and C j , is as follows:
  • if w i j > 0 , then strengthening (weakening) of the concept C i will lead to strengthening (weakening) of the concept C j with intensity w i j .
  • if w i j < 0 , then strengthening (weakening) of the concept C i will lead to weakening (strengthening) of the concept C j with intensity w i j .
  • if w i j = 0 (or is very close to 0), this indicates that there is no causal relationship between C i and C j , so there is no corresponding arc in this graph.
The final state of the system at t depends on the initial vector A 0 and the weight matrix W . The activation of the concept С i at time t + 1 is given in equation (1) and depends on the influences of the other concepts associated with the concept С i and the activation value of the concept at time t .
A i t + 1 = S j = 1 i j M ( T ( w j i , A j t ) )
where w j i is the weight of the connection between concepts j and i , A j t is the activation of the concept j at time t , T is the fuzzy operator of the triangular norm (T-norm), and S is the fuzzy operator of the triangular conorm (S-norm), which are fuzzy logic operators used to solve problems of accumulation of influence of several control concepts on the target concept and to determine the indirect influence of concepts.
The FCM update rule is applied recursively until a certain termination condition is met. At each discrete time step, the FCM will generate a matrix A t containing information about the activation degree of all concepts. In the FCM, individual fuzzy influences of control concepts that influence target concepts are combined using S-norms. T-norms and S-norm are operators in fuzzy logic that represent conjunction and disjunction operations on the interval 0 , 1 . The most well-known fuzzy logic operators are the T-norm operator minimum min ( p , q ) , which is used for the intersection operation, and the dual S-norm operator maximum max ( p , q ) , which represents the sum operation. Using the T-norm operator minimum can be advantageous for those systems in which the information processing method is close to logical, i.e. most of the dependencies between the input and output values of the system are binary in nature.
To add negative cause-and-effect relationships between the concepts of the FCM, the algorithm described by Silov [18] was used in the work. Its main idea is to create a second matrix describing all negative impacts in the system. To do this, the initial dimensions of the FCM are doubled by separating positive and negative impacts using the rule described by equation (2) to obtain a matrix R containing only positive weights.
r 2 i 1 , 2 j 1 = w i j , r 2 i , 2 j = w i j , r 2 i 1 , 2 j = 0 , r 2 i , 2 j 1 = 0 ,   i f     w i j 0 r 2 i 1 , 2 j 1 = 0 , r 2 i , 2 j = 0 , r 2 i 1 , 2 j = w i j , r 2 i , 2 j 1 = w i j , i f     w i j < 0
Given that the matrix W has the size M × M , where M is the number of concepts considered in the model, the matrix R will have the size 2 M × 2 M . Since the weight of the arcs in the FCM usually depends on expert opinion and is not exact, some of the links may be missing and/or their weight may be determined inaccurately. To adjust the weight matrix and identify hidden links between concepts, we used the probabilistic transitive closure (PTC) approach [19], which consists of calculating a bipolar weighted oriented graph with the same set of concepts as the original FCM, but with links corresponding to the indirect effects in the FCM. The link weight ( r i * , r j * ) in the PTC R * matrix is the probability that the FCM has an arc from r i * in r j * . The PTC matrix R is obtained from the matrix using Equation (3):
R * = R R
where is the PTC. After calculating the indirect effects in the FCM using PTC , the matrix R * can be reduced to its initial size M × M by obtaining the matrix V , which is formed using the transformation described in Equation (4):
v i j = max ( r 2 i 1 , 2 j 1 * , r 2 i , 2 j * ) v ¯ i j = max ( r 2 i 1 , 2 j * , r 2 i , 2 j 1 * )
where v i j and v ¯ i j represent the positive and negative impact of the concepts, respectively. The matrix V elements are used in scenario modeling and allow for problem-target analysis in complex systems.
The FCM of the electrodialysis plant was constructed using the following steps:
  • Expert interviews were conducted to identify the concepts of the FCM and the interactions between them. Using the language equivalents of “Very Low”, “Low”, “Average”, “High”, “Very High” and the direction of influence, positive or negative, experts were asked to rate the influence of one concept on another.
  • Experts' qualitative ratings were converted into a numerical equivalent (0–4) and combined using a weighted mean based on the expert's tenure.
  • The numerical values were normalized on interval [ 1 , 1 ] and a matrix W of connection strengths w i j was constructed.
  • The FCM was trained, resulting in a matrix of positive and negative relationships V = v i j , v ¯ i j .
  • The analysis of the constructed FCM was carried out and system indicators were calculated.
After training the FCM and constructing a matrix of positive-negative connections, the resulting system is analyzed. For this purpose, based on the matrix of positive-negative connections V = v i j , v ¯ i j , the system indicators of the analyzed weakly structured system are determined.
Weakly structured systems are systems in which qualitative, poorly defined concepts prevail, and the criteria for evaluating the alternatives of the decisions taken are, as a rule, of a subjective nature. The system being evaluated is a representative of this class since it includes qualitative parameters such as the quality of purification and the service life of the membrane. When analyzing system indicators - such as mutual consonance, dissonance, positive and negative influence of concepts on each other and on the system as a whole - determining key factors of the model, and conduct a scenario analysis of the system as described in [21].

3. Results

As a result of the study, the FCM of the electrodialysis plant at the water treatment facility was constructed, the analysis of positive and negative components of the links and the system analysis of the constructed FCM were carried out. Strategies to increase the efficiency of the water treatment facility were proposed.
In the initial modeling stage, potential system concepts were proposed. Expert interviews were conducted to compile a list of FCM concepts. Obtained list presented in the Table 1. During second stage of the interviews, experts assessed cause-and-effect relationships using a scale of “Not related”, “Very weakly related”, “Weakly related”, “Related”, “Strongly related”, “Very strongly related”. These assessments were converted to a 0–4 scale and averaged. A matrix representing the mutual influence weights between concepts was then constructed.
Figure 2 shows the resulting FCM as an oriented weighted graph, and Table 2a and Table 2b show the matrix of relationships between the concepts of the resulting system. The third row of the FCM matrix shows that the concept k3 (Concentration of salt ions) is negatively influenced by k1 (Solution flow rate) with a weight of –0.01 and by k7 (Membrane service life) with a weight of –0.8, while it is positively influenced by k8 (Current strength in the system) and k9 (Potential jump in the system), both with a weight of 0.8. For an illustrative example, we selected the target states of the electrodialysis plant at a water treatment facility system as:
Increase in concept k7 (Membrane service life).
Reduction of concept k16 (Power consumption (electrodialysis + pump operation)).
From the original FCM W = w i j of dimension n × n a fuzzy matrix of positive connections was formed R ( 2 n × 2 n ) . After that, a transitively closed cognitive matrix of mutual influences was calculated and the system indicators of the FCM were calculated. The system indicators were determined as described in [21] and presented in Table 3.
When analyzing the obtained model, we can conclude that the first target concept k7 (membrane service life) is weakened by the system and the dissonance of the weakening effect is below average, therefore the development trend of this concept is negative. The target concept k16 (electricity consumption of electrodialysis and pump operation) is reinforced by the system, with above-average consonance, indicating an optimistic development trend. The concept k5 (membrane conductivity) has the strongest positive influence on the system (impact: 0.219), although the system does not, in turn, reinforce this concept. The consonance of the concept is high, therefore it itself provides strengthening of the system.
The next concept in terms of the degree of positive amplification of the system is the concept k13 (channel length). The concept k19 (installation cost) is provided by the growth under the action of the system, while it has an insignificant effect on the system. The concept k14 (device productivity) is contradictory, the system increases it, and it has a strong negative effect on the system. Since the consonance of the system's influence for k14 is maximum within the framework of the considered model, there is an optimistic development trend. Among all concepts, the system most significantly weakens the target concept k7 (membrane service life).
Let us consider the clusters of positive and negative influence available in the system, taking into account the assignment of the corresponding relevance level based on the matrices of positive and negative mutual influence. This allows us to identify groups of similar concepts and analyze the relationships within the clusters of interest. Assigning relevance levels enables graphical evaluation of the clusters and accelerates matrix analysis.
In Figure 3 (left), the following clusters of mutually reinforcing concepts can be identified: k5 (membrane conductivity), k2 (water temperature at the inlet to the chamber), k14 (device performance) - form the cluster "Purification speed", which is closely related to another cluster - "Installation characteristics", including concepts k4 (purification quality), k13 (channel length), k19 (installation cost), k18 (installation size), k10 (number of paired chambers in the device). A separate cluster includes k16 (electricity consumption), along with k1 (solution flow rate), and k17 (pump efficiency). To examine contradictions within the system, Figure 3 (right) illustrates groups of opposing concepts. The first cluster is represented by concepts k11 (distance between membranes in the apparatus), k1 (flow rate of the solution), k12 (width of the inlet opening), k15 (amount of salts in the solution), k17 (pump efficiency) with an impact on concept k4 (purification quality). The second cluster, consisting of k2 (water temperature at the inlet to the chamber), k3 (salt ion concentration), k5 (membrane conductivity) has an impact on concept k7 (membrane service life).
To support decision-making, we addressed the inverse problem for FCM model of the electrodialysis plant at a water treatment facility. The methodology used to solve this problem follows the approach detailed by Petukhova et al. [22], which outlines an optimization algorithm for inverse problem modeling in FCMs. For demonstration purposes, Table 4 presents the specified increments in the values of selected target concepts used in the illustrative scenario.
Solving the problem yields a vector of control concept increments, presented in Table 5.
The results presented in Table 5 can be summarized as follows. The upper-level strategy, corresponding to the Max solution type, is primarily focused on reducing most control concepts, with the exception of k11 (distance between membranes in the device). Notably, increasing this parameter in the direct task by soling Eq. (1), leads to an overall improvement in the target concepts; however, it also causes a significant decrease in the k4 (quality of purification). In contrast, the diverse range of lower-level strategies, represented by the Min solution type, provides flexibility for experts. These strategies enable the selection of optimal control actions tailored to the specific requirements and constraints of the water treatment system.

4. Conclusion

This article presented a detailed analysis of an electrodialysis plant model at a water treatment facility using FCM theory. The model was examined, and an example was provided to demonstrate its application in decision support and the development of system strategies. The analysis revealed that the target concept, ``Membrane service life”, is weakened by the system, reflecting a negative development trend. In contrast, ``Electric power consumption” is positively influenced by the system, suggesting that its value increases in tandem with other system variables. The concept ``Electrical conductivity of membranes” was identified as the most influential factor strengthening the system, a conclusion supported by experimental data.
The study confirms the applicability of the FCM method not only to socio-economic systems but also to physicochemical systems. The developed model demonstrates that FCMs can be effectively used to monitor and control electrodialysis processes in real time by dynamically adjusting system parameters. The implementation of FCM-based decision support tools in operational settings can lead to improved process efficiency, extended membrane lifespan, and significant reductions in energy consumption and maintenance costs.
From a practical standpoint, this approach can support plant operators in identifying system bottlenecks early, optimizing resource use, and making data-driven decisions to ensure stable and cost-effective water treatment operations.
Future research could involve training the proposed model on historical and real-time experimental data using error-dependent learning algorithms. Another promising direction is the incorporation of time delays in concept influence, allowing the model to represent intermediate system states and better capture the dynamic nature of system responses.

Author Contributions

Conceptualization, A.P., A.K.; methodology, A.P.; software, A.P.; validation, A.P., A.K.; formal analysis, A.P.; investigation, A.P.; resources, E.K.; data curation, A.P.; writing—original draft preparation, A.P.; writing—review and editing, E.K.; visualization, A.P.; supervision, E.K.; project administration, A.K. All authors have read and agreed to the published version of the manuscript.

Funding

This research was funded by the Russian Science Foundation, research project No. 24-19-00648, https://rscf.ru/project/24-19-00648/.

Conflicts of Interest

The authors declare no conflicts of interest.

Abbreviations

The following abbreviations are used in this manuscript:
ANN Artificial neural networks
ED Electrodialysis
EMS Energy management system
FCM Fuzzy Cognitive Map

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Figure 1. Example of a simple fuzzy cognitive map.
Figure 1. Example of a simple fuzzy cognitive map.
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Figure 2. FCM of electrodialysis plant at water treatment facility.
Figure 2. FCM of electrodialysis plant at water treatment facility.
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Figure 3. On the left - mutual positive influence of the concepts with selected cutoff level of 0.85 with operator max – min. On the right - mutual negative influence with selected cutoff level of 0.6 with operator max – min.
Figure 3. On the left - mutual positive influence of the concepts with selected cutoff level of 0.85 with operator max – min. On the right - mutual negative influence with selected cutoff level of 0.6 with operator max – min.
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Table 1. Concepts included in the model of an electrodialysis plant at a water treatment facility.
Table 1. Concepts included in the model of an electrodialysis plant at a water treatment facility.
Designation Concept Concepts type
Solution flow rate k1 State
Water temperature at the inlet to the chamber k2 State
Concentration of salt ions k3 State
Quality of purification (degree of desalination) k4 State
Electrical conductivity of membranes (membrane resistance) k5 State
Regeneration frequency k6 Exogenous
Membrane service life k7 Endogenous
Current strength in the system k8 State
Potential jump in the system k9 State
Number of paired chambers in the device k10 State
Distance between membranes in the device k11 Exogenous
Width of the inlet opening k12 Exogenous
Channel length k13 State
Device performance k14 State
Concentration of salts in the solution k15 Exogenous
Power consumption (electrodialysis + pump operation) k16 Endogenous
Pump efficiency k17 Exogenous
Unit size k18 State
Unit cost k19 State
Table 2a. Matrix of FCM of electrodialysis plant at a water treatment facility (for k1..k11).
Table 2a. Matrix of FCM of electrodialysis plant at a water treatment facility (for k1..k11).
Concept k1 k2 k3 k4 k5 k6 k7 k8 k9 k10 k11
k1 0 0 0 -0,6 0 0 -0,4 0 0 0 0
k2 0 0 0 0,8 0 0 -0,7 0 0 0 0
k3 -0,01 0 0 0 0 0 -0,8 0,8 0,8 0 0
k4 0 0 0 0 0 0 0 0 0 0 0
k5 0,5 0 0 0 0 0 -0,6 0,8 0,8 0 0
k6 0,3 0 0 0,8 0 0 0,8 0 0 0 -0.6
k7 0 0 0 0 0 0 0 0 0 0 0
k8 0,02 0,3 0 0,7 0 0 -0,5 0 0 0 0
k9 0,02 0,3 0 0,7 0 0 -0,5 0 0 0 0
k10 0 0 0 0,9 0 0 0 0 0 0 0
k11 0 0 0 -0,6 0 0 0 0 0 0 0
k12 0,8 0 0 0,8 0 0 0 0 0 0 0
k13 0,2 0 0 0,75 0 0 0 0 0 0 0
k14 0 0 0 -0,4 0 0 0 0 0 0 0.2
k15 0 0 0 -0,7 0 0 0,75 0 0 0 0
k16 0 0 0 0 0 0 0 0 0 0 0.1
k17 1 0 0 0 0 0 0 0 0 0 0
k18 -0,05 0 0 0 0 0 0 0 0 0 0
k19 0 0 0 0 0 0 0,4 0 0 0 0
Table 2b. Matrix of FCM of electrodialysis plant at a water treatment facility (for k12..k19).
Table 2b. Matrix of FCM of electrodialysis plant at a water treatment facility (for k12..k19).
Concept k12 k13 k14 k15 k16 k17 k18 k19
k1 0 0 0,8 0 0,6 0 0 0
k2 0 0 0,9 0 -0,2 0 0 0
k3 0 0 -0,1 0 0,2 0 0 0
k4 0 0 0 0 0,3 0 0 0
k5 0 0 0,9 0 -0,2 0 0 0,4
k6 0 0 0 0 0,2 0 0 0
k7 0 0 0 0 0 0 0 0
k8 0 0 0,6 0 0,7 0 0 0
k9 0 0 0,6 0 0,7 0 0 0
k10 0 0 1 0 0,7 0 0,9 0,8
k11 0 0 0,2 0 0,1 0 0 0
k12 0 0 0,3 0 -0,1 0 0 0,2
k13 0 0 -0,4 0 0,4 0 0,7 0,9
k14 0 0 0 0 0,2 0 0 0
k15 0 0 0 0 0,3 0 0 0
k16 0 0 0 0 0 0 0 0
k17 0 0 0 0 0 0 0 0,8
k18 0 0 0 0 0,6 0 0 0,9
k19 0 0 0 0 0 0 0 0
Table 3. System characteristics of a FCM used in the analysis of the electrodialysis plant at a water treatment facility.
Table 3. System characteristics of a FCM used in the analysis of the electrodialysis plant at a water treatment facility.
Concept Consonance of the influence of the system Consonance of the influence of the concept The influence of the system on the concept The impact of the concept on the system
k5 0 0.383 0 0.219
k11 0 0.12 0 -0.031
k13 0 0.272 0 0.154
k14 0.632 0.066 0.354 -0.011
k19 0.316 0.053 0.211 0.021
k7 0.613 0 -0.065 0
k16 0.487 0 0.369 0
Table 4. Target concept increments.
Table 4. Target concept increments.
Concept Concept augmentation Consonance of the influence of the concept
k7 0.1 0.4
k16 -0.1 0.6
Table 5. Target concept increments.
Table 5. Target concept increments.
Solution type k3 k5 k6 k10 k11 k12 k13 k15 k17
Max -0.125 -0.125 0 -0.132 0.250 -0.174 0 0 -0.134
Min -0.125 0 0 -0.132 0 0 0 0 0
Min -0.125 0 0 -0.132 0.250 0 0 0 0
Min -0.125 0 0 -0.132 -0.139 0 0 0 0
Min -0.125 0 0 -0.132 0 0.052 0 0 0
Min -0.125 0 0 -0.132 0 -0.174 0 0 0
Min -0.125 0 0 -0.132 0 0 0 0 0.042
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