Implementation and Evaluation of Physical, Hybrid, and Virtual Testbeds for Cybersecurity Analysis of Industrial Control Systems

Abstract

Industrial Control Systems are an essential part of our daily lives and can be found in industries such as oil, utilities, and manufacturing. Rapid growth in technology has introduced industrial components with network capabilities that allow them to communicate with traditional computer networks, thus increasing their exposure to cyber-attacks. Current research on Industrial Control Systems suffer from lack of technical information as these systems are part of critical infrastructures. To overcome this, researchers have employed different types of testbeds to develop their mechanisms of cyber-attack detection and prevention. This manuscript describes, implements, and evaluates physical, hybrid, and virtual application of a clean water supply system developed for cybersecurity research. The results show that physical testbeds allow an understanding of the behaviour and dynamics of control components like sensors and actuators, which might be affected by external influences such as noise, vibration, temperature, and non-ideal device behaviour. Although, hybrid testbeds reduce the cost of implementation, they ignore the physical dynamics of the system as explained above. Virtual testbeds are the cheapest option in comparison with physical and hybrid testbeds; however, they provide a limited view of the control system operation that could have negative consequences when developing a detection/prevention system.

1. Introduction

Industrial Control System (ICS) is a general term used to define the integration of hardware and software with network connectivity used to operate industrial processes [1]. ICS often includes Supervisory Control and Data Acquisition (SCADA) systems, Distributed Control Systems (DCS), and different control system configurations such as Programmable Logic Controllers (PLC). PLC can be found in industrial sectors and critical infrastructure such as oil, pharmaceutical, power plants, and water distribution systems. These industrial sectors contribute to the economy of a country and are an essential part of the daily services used by citizens. For instance, there are 13 critical national infrastructure sectors (such as: water, transport, chemical, space, food, defence, government and civil nuclear) identified in the UK, which are important for the operation of the country [2] and whose possible compromise might involve the loss of human lives. In the US, Homeland Security [3] defines 16 critical infrastructure sectors (such as: dams, emergency services, information technology, commercial infrastructure, critical manufacturing, and communications) as fundamental pillars for the operation of the country, whose damage might have devastating consequences on the public, economy, and environment. In general, the US and the UK focus on the same critical infrastructure and the difference is on the classification of such infrastructure.

Control system technology has grown in leaps and bounds over the past decades allowing to evolve from mechanical through electrical/electronic to microprocessor-based systems. This evolution has increased the connectivity of ICSs with corporate networks and the Internet. As a result, old industrial infrastructures with unpatched systems are exposed to skilled hackers that can easily take advantages of their online availability. For instance, in 2010 the Stuxnet worm demonstrated the vulnerabilities of ICSs and their potential threat when a malware destroyed a considerable amount of Iran’s nuclear centrifuges [4].

ICS have attracted the attention of cybercriminals because it is composed of old equipment with obsolete or no security measures. For example, a considerable number of computers involved in ICS operations still run on older operating systems, such as Windows XP or Windows 7, without the latest patches. According to the report published in [1] this is attributed to the uncertain results of applying security patches despite its security benefits. IT systems benefit from the flexibility that virtualization provides. It enables the latest security patches to be applied to a virtual copy of any computer before it is applied to productive systems. This allows evaluating the impact of security patches on the system and applications in case their normal operation is affected. In contrast, the cost of replicating an ICS is considerably high because it involves purchasing expensive control equipment and having physical space available. For example, industries such as oil, nuclear, and water cannot afford to implement a control process to test only for security patches. However, as demonstrated in this research, it is possible to downscale a model of an ICS on equipment that may be available in University laboratories. Throughout the investigation we compare the differences in implementations of physical and virtual control systems. Each of the approaches has its advantages and disadvantages as discussed throughout this paper.

1.1. Research Questions

The experiments conducted in this paper aim to describe the advantages and disadvantages of using physical, hybrid, or virtual testbeds for cybersecurity research on ICS. The research questions that will be answered in the course of this paper are as follows.

Research Question 1. How does a hybrid and virtual implementation of a clean water supply system differ during normal operation and under attack scenarios in comparison with the physical model of such a system?

Research Question 2. Can we rely on mechanism of anomaly detection on ICS which are developed and tested on virtual platforms?

1.2. Contribution

In this paper, a cybersecurity analysis of a physical, hybrid and virtual testbed that simulates a clean water supply system is discussed. A set of attacks against the working memory of the PLC is executed aiming to analyse the behaviour of such attacks on the implemented testbeds. The results show the strengths and weaknesses of each approach.

1.3. Organization of the Paper

This paper is organised as follows: In Section 2, we review related work with a focus on testbeds for ICS cybersecurity research. In Section 3, we describe the design and implementation of the three testbeds presented in this research. In Section 4 the testbeds are evaluated by highlighting their strengths and weaknesses. In Section 5, we discuss the research questions stated at the beginning of the paper and, finally, in Section 6, we present the research findings. The references used in this research are listed at the end of the paper.

2. Related Work

Most of the current research approaches are dedicated to detecting anomalous activities on ICSs based on publicly available datasets such as [5,6] either by having direct access to the physical testbed and the dataset or only to the dataset itself. However, these datasets become obsolete when new attacks arise due to the rapid evolution of the malware industry. Researchers also use tools such as MATLAB to build simulation environments that fully mimic the behaviour of a real ICS. Moreover, another cost-effective approach involves implementing hybrid testbeds that include control hardware such as PLCs along with virtual simulations. Thus, the following literature focuses on describing the physical, hybrid, and virtual testbeds available for research. We intend to focus on the control process that encompasses water systems or similar processes, as they are related to the testbeds implemented in this paper.

2.1. Physical Testbeds

An ICS physical testbed is a scaled-down version of a control system. It includes physical equipment such as PLCs, and sensors/actuators that are currently used in the industry. The ICS physical testbeds described as follows are the most popular among academia.

The Secure Water Treatment (SWaT) testbed [7] is one of the most used testbeds among researchers. This is a scaled-down water treatment plant that produces five gallons/minute of doubly filtered water. The water treatment process involves six stages each controlled by an independent PLC. Each PLC receives information from sensors connected to the corresponding stage, processes the information and controls actuators like pumps and valves in its domain. The SWaT testbed comprises of a layered communication network, SCADA systems, Human Machine Interface (HMI), and Historian Data. The SWaT dataset involves 11 days of continuous operation, 7 days under normal operation, followed by 4 days of attacks against the control process. This includes 36 scenarios of single-point, multi-point, man in the middle, packet hijacking, single-stage, and multi-stage attacks. The entire set of attacks is conducted through the network in a controlled environment. However, accessing this testbed is rather difficult and the researchers are dependent on the datasets generated by its creators.

The FACIES testbed is another scaled-down water system developed within the eponymous EU Project [8]. The main aim of this testbed is to contribute to the analysis and identification of cyber threats targeting Critical Infrastructure. FACIES includes three layers; Layer 0, which comprises 5 sensors and 24 actuators, Layer 1, which contains two PLC, and then Layer 3, which embraces a SCADA system and a Human Machine Interface (HMI). The dataset obtained from this testbed contains normal and anomalous operation. The set of attacks performed against the testbed includes man-in-the-middle, ARP spoofing, and packet hijacking. However, these attacks are rather simplistic, and they have already been tackled by security devices such as firewalls and Intrusion Detection Systems (IDS) for many years. Generally speaking, today’s network is not vulnerable to these attacks anymore.

In the same way, the researchers in [6] introduce Water Distribution (WADI) which is a water distribution testbed for research. It represents a scaled-down version of a water distribution network that can be found in a small city. The water distribution process involves three stage of: purification, distribution, and recycling. WADI is composed of three layers as follows. Layer 0, which contains sensors/actuators and I/O modules using RS845-Modbus Protocol. The PLCs connected to a central node is in layer 2 while HMI and the plant control network are in layer 3. The main limitation of the WADI testbed is that the researchers only implemented spoofing attacks which are rather simplistic. This reduces the opportunity of investigating the behaviour of the system under more sophisticated attacks.

In [9], the researchers introduce a SCADA testbed built for cybersecurity and forensics research. The testbed simulates a gas pipeline, a power distribution system, and a water treatment process. We focus on the last process (i.e., water treatment) since it is more related to our work. Their water treatment process includes three sets of tanks lined up in sequence, water pump, Siemens PLC S7-300, and sensors that provide the water level in each tank. Additionally, there is a HMI interface that allows monitoring and controlling the control process. Their attack vectors include the analysis and exploitation of vulnerabilities in industrial protocols such as Modbus/Transmission Control Protocol (TCP) and Profinet. However, the implementation of the cyberattacks to the control process is rather unclear. Further, in the testbed, the researchers did not use sensors/actuators that could be found in the industry, instead, they used small components intended for pedagogical use. Additionally, the PLC used in this testbed has well-known vulnerabilities such as sensitive data disclosure which have been explored before [10].

2.2. Hybrid Testbeds

Vulnerability assessment on physical testbeds provides the most accurate results; however, the cost of implementing such a system is considerably high. Hybrid testbeds try to address the trade-off between cost and implementation by virtualizing some components such as sensors and actuators. Other components like PLC and HMI remain physical.

In [11] the researchers provide a hybrid testbed that simulates a non-linear process called the Tennessee Eastman (TE) chemical process. It is composed of five operating units which are: a reactor, a product condenser, a vapour-liquid separator compressor and a stripper. The testbed integrates hardware such as a PLC and a virtual model simulated in MATLAB. The PLC communicates with the process through a serial cable. The main drawback of this testbed is that software cannot simulate the fast dynamics of some components such as sensors and actuators. Furthermore, the set of attacks performed in this testbed are represented in mathematical equations. Therefore, it is not clear whether the chosen attacks can be replicated in a real environment.

In [12], the researchers provide a hybrid implementation of an electrical grid. The simulated process is a regional-scale energy distribution network using specialised proprietary software. They implement a Modbus TCP/IP communication between the PLC and the simulated process that resides in a virtual computer. This allows monitoring and analysing the network traffic aiming to discover new vulnerabilities. The set of attacks against this testbed includes network reconnaissance, ARP Spoofing, and man-in-the-middle. It is worth noting that the researchers used Modbus TCP/IP protocol vulnerabilities to cause disruptions to the control process. Additionally, the set of attacks executed against this testbed is rather simplistic and limited to network-based attacks.

In [13] the researchers propose VTET: A virtual control system testbed for cybersecurity research. This testbed has 2 operational modes: hybrid mode and virtual mode. The virtual process used in this testbed is the TE chemical process described above. In VTET, the main difference between both modes is that the PLC is physical when the testbed operates in hybrid mode but replaced by a PC in virtual mode. Furthermore, the virtual testbed operates with two protocols such as Open Platform Communications (OPC)/S7, while in hybrid mode adds support for the Modbus TCP/IP protocol. The set of attacks employed by the researchers are executed at the network level which includes reconnaissance and Denial of Service (DoS). Additionally, while the researchers claim that a set of sophisticated attacks against the PLC program are executed, the implementation of those attacks are rather unclear. Moreover, the execution of DoS attacks might be impractical in a real-world scenario given that the amount of traffic generated in such scenario might not be the same when it is executed in a virtual environment.

In [14], the researchers provide a hybrid implementation of a water distribution system. The testbed is composed of a Siemens S7-400 PLC which is integrated with a virtual remote terminal unit (RTU). The communication between both components is through Modbus TCP/IP. The virtual RTU contains the entire simulation environment which includes two tanks, a two-level sensor and one pump. The network traffic generated by the virtual plant is simulated using tcpdump. The set of network attacks implemented involves typical and rather simplistic network attacks such as DoS and TCP Spoofing. Given that the working memory of the Siemens S7-400 PLC is not optimised, the work could have benefitted from executing more harmful cyberattacks against the system rather than just DoS and TCP Spoofing.

2.3. Virtual Testbeds

A Virtual ICS testbed simulates the entire components that creates a complete control system. A virtual testbed allows understanding of the operation of an ICS without physical or hybrid implementations, for example, without the need to buy any physical components such as PLC, and sensors/actuators.

In [15], the researchers propose a virtual SCADA testbed for research. The system simulates a simple water tank system, and it is developed on Common Open Research Emulator (CORE). This testbed uses a light version of the Linux virtualisation system and python for simulating each testbed component. It implements instrumentation devices like sensors and valves, Remote Terminal Unit (RTU), Master Terminal Units (MTU), HMI, and control equipment such as the PLC. Modbus TCP is used as a communication protocol between the components that have network capabilities. Distributed Denial of Service (DDoS) and Man-in-The-Middle attacks are virtually developed to test against this testbed. Given that the implemented attacks are rather simplistic, it is not clear whether it is possible to implement more sophisticated attacks that involve components such as the PLC or HMI.

In [16], the researchers introduce SCADAVT-A a framework for building a SCADA testbed for cyber-security research. The testbed simulates a water distribution system using EPANET [17] a specialised software for simulating pipe networks. Their simulation environment includes three water tanks that distribute water into specific areas of a town, a PLC, and an HMI client. They used Modbus TCP as the network communication protocol. The attack scenarios executed against the testbed are limited to DoS and Man-in-The-Middle. It should be noted that these attacks are easily executed due to vulnerabilities presented in the Modbus TCP protocol. Furthermore, current security devices such as firewalls and IDS are fully able to detect and prevent such attacks before they reach/compromise the control system.

In [18], the researchers present a virtual implementation of a water purification plant. The testbed is composed of a virtual PLC, HMI, a tank, a heater, two valves, a level sensor, and a temperature sensor. This testbed is implemented using C++ as a programming language, Bro, as a packet extractor, and Modbus TCP as a network communication protocol for ICS. The researchers employed network-based attacks, such as DoS, Man-in-The-Middle, and reconnaissance and control process attacks. Attacks against the control process aim to tamper the values collected from sensors/actuators. It should be noted that both group of attacks are executed at the network level. This means the attacker requires access to the network packets before the control process values can be manipulated.

In [19], the researchers introduce TASSCS: a virtual testbed created for analysing the security of SCADA Control Systems. The testbed involves three zones as follows. (1) Process Control Zone, which involves the main control and management services for the SCADA system, (2) Demilitarised Zone (DMZ), which manages requests from the corporate zone and (3) Corporate Zone which comprises of corporate clients. The attack scenarios targeting vulnerabilities in the Modbus protocol aiming to tamper with the communication between the PLC and the SCADA system. Additionally, attacks such as Man-in-The-Middle and DoS are implemented. It should be noted that the simulation proposed by the researchers require a significant amount of computing capabilities. Furthermore, it is argued whether a virtual DoS attack can have the same behaviour in a real-world case scenario.

In this paper, the implementation and evaluation of virtual, hybrid, and physical testbeds that simulate a scaled-down version of a Clean Water Supply System (CWSS) are provided. The testbeds are named Clean Water Supply System- Physical (CWSS-P) for the physical implementation, Clean Water Supply System- Hybrid (CWSS-H) for its hybrid version and Clean Water Supply System- Virtual (CWSS-V) for the virtual representation. The CWSS-P involves a physical S7-1500 PLC and a model of a clean water supply system implemented in the Festo rig. The CWSS-H employs a virtual version of the Festo rig, which is designed and implemented in MATLAB along with a real S7-1500 PLC and a physical OPC Server. In CWSS-V, we virtually implement the whole CWSS in MATLAB. The evaluation of the three testbeds is made during normal operation and under different attack scenarios. Unlike [7,8,9,14] our CWSS-P and CWSS-H employ a cutting-edge S7-1500 PLC which is currently used in the industry. Moreover, the set of attacks executed against the testbeds exploit vulnerabilities at the input/output/working memory of the PLC, which differ from the network-based attacks executed in [7,8,11,12,13,14,15,16,17,18,19]. The next section describes the design and implementation of our testbeds.

3. Testbed Design and Implementation

This section describes the design and implementation of the physical, hybrid, and virtual testbeds for cyber-security analysis of Industrial Control Systems. The architecture of these testbeds is designed according to the guidelines described as follows.

3.1. ICS Architecture

ICSs are composed of different elements such as electrical, mechanical, and pneumatic that are used to achieve various objectives in industries like manufacturing or transportation. There are several guidelines, security standards, and best practices on ICS risk management. For example, IEC/ISA-62443 [20], which is an ICS security standard, or the UK’s CPNI [21], which provides a practice guide for ICS security. As the researchers in [22] state, and we also agree, two important guides that describe the ICS architecture are NIST 800-82 [23] and the Purdue model suggested by SANS [24]. The representation of these two architectures is shown in Figure 1.

Figure 1. Industrial Control System (ICS) Architecture: (a) 1 Purdue Model for Control Hierarchy logical framework; (b) ICS reference model.

The Purdue Model for control hierarchy logical framework provides a more detailed classification in comparison with the NIST model. Purdue model identifies four zones and six levels as it is depicted in Figure 1. The Safety Zone is an air-gapped system that alert operators about unsafe conditions. The Cell/Area Zone is defined as a functional area within a production facility while the Manufacturing Zone comprises the Cell/Area networks and site-level activities. The Enterprise Zone is where business systems such as Enterprise Resource Planning (ERP) and System Applications and Products (SAP) typically reside. Each zone has a sub-classification represented as levels and each level is a logic segment of an ICS that performs a specific function.

NIST states that an ICS should focus on four general areas: the control centre, the communication architecture, the field devices, and the physical process itself. Figure 1 shows the ICS reference model suggested by NIST. Level 0 includes hardware such as sensors that compose the control system, while Level 1 involves control equipment such as PLCs. At Level 2, equipment that monitors and control the operation of the process such as SCADA system and HMI resides, whereas the corporate network is part of Level 3.

Purdue Model includes a safety zone which is not described in the SANS model. Both models include HMI in addition to other equipment at Level 2, but it does not comprise of SCADA systems given that they belong to Level 3. In both models, Level 0 includes sensors and actuators that are connected to the physical process. For instance, ultrasonic sensors, flowmeters, pressure sensors, valves, and pumps can be found in Level 0. Level 1 involves equipment that controls sensors and actuators found at the previous level (i.e., Level 0). For instance, devices such as PLC are placed at Level 1. The PLC receives information from the physical process through hard-wired sensors, then it processes such information using control techniques like Proportional Integral Derivative (PID), The Cascade, and Feed Forward. Finally, it controls actuators like pumps and valves.

3.2. Virtual Plant

The virtual plant developed for this research simulates the operation of the physical process implemented in the Festo rig. To achieve this, we use Simulink [25] which is a MATLAB graphical editor for modelling and simulating dynamic systems. Figure 2 shows the virtual representation of the Festo Rig, and its physical components. The virtual plant is composed of elements with the same characteristics and properties as the physical components. To achieve such similarity, we built the virtual sensors/actuators from the information obtained from the Festo Rig datasheet [26]. The virtual plant elements are as follow.

Figure 2. Hybrid testbed: (a) CWSS virtual process; (b) Festo rig components.

Pipes: The diameter of the pipes used in the virtual model is 18.621 mm.

Pressure Vessel: The pressure vessel acts as a normal pipe; however, its shape causes a small drop in the water pressure. We model this component as a sudden change in the pipeline. The diameter of both ends corresponds to the diameter of the pipe, which is 18.621 m. The diameter at the centre of the pressure vessel is calculated using the Equation (1). The volume (Vol) is obtained from the Festo rig datasheet, while h represents the height of the vessel.

$$d= \sqrt{\frac{Vol}{\pi h}}$$

(1)

Pump: The virtual pump is composed of several components. A motor controller which supplies a voltage in the range of 0 to 24 volts, a DC Motor, and a centrifuge pump.

Proportional Valve: The proportional valve simulates the water demand of a town. The virtual valve operates with the same water demand models implemented in the physical valve. It is implemented as a variable orifice valve. Its range of operation is determined during the experimentation phase.

Water Tanks: The water tanks have a variable cross-section area. The first step is to obtain the measurements of the physical tanks. Then, the virtual tanks are created from these measurements.

Flowmeters: The physical flowmeters are represented as hydraulic flow rate sensors.

Ultrasonic Sensor: The ultrasonic sensor is not implemented in the virtual testbed. The virtual tanks provide its fluid level.

3.3. Physical Testbed (CWSS-P)

The CWSS testbed physically models a continuous clean water supply system using a custom configuration of the Festo MPS PA Compact Workstation Rig [26] shown in Figure 2. This testbed distributes its components in three levels, according to the ICS reference model shown in Figure 1.

Layer 0 comprises of sensors/actuators involved in the physical process. These devices are described as follows:

• One Ultrasonic sensor.
• Two Flowmeters.
• Two Pressure Sensors.
• One Pump.
• One Solenoid Valve.
• One Proportional Valve.

Level 1 involves a Siemens S7-1500 PLC [27] that is used to control the system operation by using the information provided by the sensors located at Level 0.

Level 2 includes equipment that monitors the status of the process through the information provided by the PLC. The equipment used to test and exploit vulnerabilities are also in this level. This equipment is described as follows:

• SCADA system running Windows 10.
• Siemens HMI.
• An attacker machine running Kali OS.

3.3.1. Normal Operation

In normal operation, the tank B102, shown in Figure 3, represents a reservoir of water to be maintained at a specified level. The tank B101 contains the water supply simulating the natural water table and feeds tank B102 through the variable speed pump (P101). Unlike the existing research, the CWSS testbed implements a set of daily water demand models using the proportional valve (V106). This allows us to implement a more realistic testbed. Further information regarding this water demand model is fully described in our previous work [28].

Figure 3. Physical testbed diagram: (a) Festo MPA Process Control Rig.; (b) Festo MPA Process Control Rig Diagram.

3.3.2. PLC Programming

PLC coding is an important task. The proper design and implementation guarantee the correct operation of the system. At the same time, it can hugely contribute as a layer of protection against intruders. As described in our previous work [28], the PLC contained an embedded mechanism of cyberattack detection and response. Among those, this testbed implements PID, Cascade and feedforward controller described as follows in addition to Table 1.

Table 1. Control techniques implemented at the CWSS testbed.

Control Technique	Sensor (s)	Tag
PID	Ultrasonic sensor	LIC/B101
PID	Pressure out	PI/105
Cascade	Flow In/Ultrasonic sensor	FIC/B102–LIC/B101
Cascade	Flow In/Pressure out	FIC/B102–PI/105
FeedForward	Flow In/Flow Out	FIC/B102–FIC/B103

PID Controller: The PID controller is an instrument used in industrial control applications and consists of three basic control actions: proportional, integral, and derivative to regulate temperature, flow, pressure, speed, and other process variables. (OP) [29].

Cascade Controller: Cascade Control is an advanced PID implementation that can improve ICS that are subject to significant delay. [1].

Feedforward Controller: Feedforward control systems measure the disturbance and modify the controller output before the process variable has time to respond. For this to be successful, the designer is required to understand how the disturbance will affect the process variable [30]. Sensors and tags can be found in Figure 3.

3.4. Hybrid Testbed (CWSS-H)

Figure 4 shows the hybrid testbed architecture. It adopts the three levels explained at the physical testbed, the main difference is that sensors/actuators that compose the Festo rig are simulated in MATLAB.

Figure 4. CWSS-H testbed architecture.

Therefore, the virtual testbed is located at Level 0. The Siemens S7-1500 PLC receives information from the virtual sensors and commands the speed of the virtual pump through the OPC server. To allow such communication, it is required to disable the memory optimisation feature in the PLC. The main issue found when disabling memory optimisation is that with disabling the memory optimisation intruders can access and manipulate those spaces of memory. This configuration makes the hybrid system more vulnerable compared to the physical system. Our previous work shows the importance of features like memory optimisation and how they prevent unauthorised memory access [28].

OPC Server and Client

OPC is a software interface standard that allows communication between industrial equipment and computers [31]. The implementation of OPC specifications involves two parts: OPC Server application and OPC client application. The OPC server obtains information from PLC and sends it back to OPC client application using the standard OPC protocol. In our hybrid testbed, the OPC toolbox [32] in MATLAB sends the virtual tank level to the OPC server. This value is used in the physical PLC as the Process Variable (PV) for the Proportional-Integral PI controller that calculates the required speed of the virtual pump. The OPC server recovers this value and the water demand from the PLC working memory. These values are sent back to the OPC client in MATLAB. The communication between the PLC, OPC Server, and MATLAB is through the OPC protocol that runs over the TPC/IP network.

3.5. Virtual Testbed (CWSS-V)

The CWSS virtual testbed (CWSS-V) is entirely implemented in MATLAB. In comparison with the physical and hybrid testbeds, the virtual testbed is composed of two levels. Level 0 includes the virtual sensors/actuators while the PLC is replaced by the PI controller at Level 1. Figure 5 shows the virtual testbed. The virtual control process is the same used in the hybrid testbed. The input parameters are the speed of the pump, which is given by the PI controller. Another input is the water demand, which is generated by a tool called: Signal Builder. The PI controller uses the same values of proportional and integral used in the physical PLC, while the signal builder replicates the water demand model used in the previous testbeds CWSS-P and CWSS-H.

Figure 5. CWSS-V testbed.

The virtual representation of this testbed, shown in Figure 5, was derived using MATLAB tools in the form of a Transfer Function (TF). This was achieved by interfacing MATLAB to the testbed using an OPC server to stimulate the real test rig via the pump and observe its response. From spotting these replies, MATLAB can estimate the system behaviour in terms of a mathematical representation of the system dynamics in the frequency domain using the Laplace operator. This operator is given by the divergence of the gradient of a function on Euclidian space [25]. The TF defines the relationship between the system output (tank level) in response to the input stimuli (pump speed command) i.e., open loop. The TF models all the physical system components mathematically. The derived transfer function of our system is a sixth-order polynomial as shown in Equation (2).

$$\frac{2.603e^{13}}{s^6+5.397e^{05}{s}^6+4.468e^{10}{s}^4+7.113e^{13}{s}^3+1.608e^{16}{s}^2+1.184e^{16}s+1.436e^{13}}$$

(2)

We can fully simulate the closed-loop response by adding a mathematical model of a Proportional Integral (PI) controller as shown in Figure 6. This allows us to evaluate the closed-loop response of the system.

Figure 6. CWSS Transfer Function.

4. Testbed Evaluation

This section shows the evaluation of our three testbeds (CWSS-P, CWSS-H, and CWSS-V) from the cyber-security perspective.

4.1. Attack Scenarios

The evaluation of the physical and hybrid testbeds against cyber threats is performed by assuming that an attacker has access to the control network. In our scenario, the attacker has gained access at Level 1 of the ICS architecture. The attacker crafts ISO 8073/X.224 COTP packets and sends over the TCP/IP network aiming to overwrite fixed spaces of memory in the PLC [33]. These novel attacks are fully explained in our previous works [34,35]. The attacks used to evaluate the physical and hybrid testbeds are performed against the input and working memory of the PLC. The values modified belong to the ultrasonic sensor at the input memory and setpoint at the working memory. Those attacks cannot be executed on the virtual testbed given that it does not have a physical PLC; however, for evaluation purposes, we mimic those attacks by tampering the values of feedback of the PI controller in the virtual testbed. This clearly points out one of the limitations of virtual testbeds.

4.2. Physical and Hybrid Testbeds

The CWSS-P and CWSS-H testbeds are executed at the same time aiming to compare their performance during normal operation and under attack scenarios. Figure 7 shows the monitoring of the process variable (setpoint) of CWSS-P and CWSS-H testbeds during both operations.

Figure 7. CWSS-P and CWSS-H during normal operation and attack conditions.

Moreover, the grey area in Figure 7 shows the normal operation of CWSS-P and CWSS-H testbeds. The setpoint of the virtual and physical tank in both testbeds remains steady during normal conditions. This demonstrates that the virtual model of the Festo Rig performs like the physical rig during normal operation. Furthermore, Figure 7 shows the behaviour of the testbeds when two attacks were executed against the input memory and working memory of the PLC. Attack 1 represents a sudden change in the working memory addressed to the setpoint. When the setpoint changes both testbeds have almost the same response. The main difference between them is positive and negative overshoot. The response of the CWSS-H testbed has more linearity than the CWSS-P. This can be attributed to the hybrid testbed being mathematically built in MATLAB, while the physical components of the CWSS-P have dynamics that cannot be simulated. After the execution of Attack 1, the system returns to the initial setpoint. This change is shown in Figure 7 with the label Back N.O.

Attack 2 shown in Figure 7, denotes the attack executed against the space of memory addressed to the input memory of the PLC. The attacker modifies the values of the physical and virtual level sensors, as a result, the water level in the physical and virtual tanks changes. During the execution of this attack, the behaviour of the CWSS-P and CWSS-H testbeds differs. The reason for this behaviour difference is because the CWSS-H testbed does not take the PI values directly from the PLC, instead it retrieves it from the OPC server. This adds a small delay in the control process that is not significant for its operation, but it represents a serious threat when the process is under attack because sensitive values such as the tank level can be modified. As shown in Figure 7, the execution of attack 2 on the CWSS-H testbed results in an overflow or emptying of the virtual tank 102. Attack 2 executed on the CWSS-P testbed produces an increase/decrease of the water level at the physical tank 102. Although the attack does not show the same behaviour as the one shown in CWSS-H, this can affect other components of the CWSS-P testbed such as the pump. The change of the setpoint during the attack is given by the sudden change of speed in the pump. If the attack continues indefinitely, the pump might overheat and stop its operation, which will affect the entire control process.

4.3. Virtual Testbed

The grey area shown in Figure 8 represents the normal operation of the CWSS-V while the arrows point to the two attacks executed against the setpoint during the operation of the system. On the same Figure, the red dotted line represents the water level at the virtual reservoir tank and the blue line denotes the output of the PI controller, which is the input voltage that regulates the pump speed. The first attack executed increases the setpoint by 2 L, which also produces a sudden increase in the output of the PI controller as it can be seen in Figure 8. This is because the controller detects a mismatch between the current water level and the new value entered by the attacker in the system. As a result, the PI controller increases its output, which represents the pump speed, until it reaches the new setpoint.

Figure 8. CWSS Virtual Plant Normal Operation.

In the second attack, in Figure 8, the intruder decreases the setpoint by 6 L. The controller output is reduced to 0 because the current water level exceeds the setpoint set by the attacker. As a result, the pump stops its operation until the new setpoint is reached.

The time it takes to arrive at this new setpoint depends on the demand for water at that time. At the end, the system returns to its normal setpoint. Figure 9 shows a closed-loop control system composed of the transfer function that represents the CWSS virtual process and a PI controller. The dotted line represents the setpoint, while the continuous line represents the output of the PI controller. The grey area represents the normal operation of the system. The operation of the system is completely linear. This is a result of the fact that the closed-loop control system only takes an input parameter, which is the output of the PI controller. Parameters such as water demand are ignored in this simulation.

Figure 9. CWSS Transfer function.

Further, in Figure 9, the controller’s output does not change during normal system operation. It only changes when the attacks are executed. In Attack 1, the intruder increases the setpoint, which produces an immediate change in the output of the PI controller until the new setpoint is reached. The intruder decreases the setpoint of the system in attack 2. The output of the PI controller is reduced to zero until the new setpoint is established. The discharge of the tank is linear due to the fact this simulation does not implement water demand models.

5. Discussion

This section addresses the research questions raised at the beginning of this paper, as well as compares the testbeds implemented in this research with the related work detailed in Section 2.

5.1. Research Questions

Research Question 1. How does a hybrid and virtual implementation of a clean water supply system differ during normal operation and under attack scenarios in comparison with the physical model of such system?

According to the results obtained from the experimentation described in this paper, the CWSS-H testbed has the same performance as the CWSS-P testbed under normal conditions and when the first attack to the setpoint is executed. This performance can be seen in Figure 7. However, in the second attack, when the intruder modifies the input memory of the PLC, the behaviour of the CWSS-H testbed differs from the CWSS-P testbed. The delay that the OPC server adds to the CWSS-H testbed allows the attacker to take full control of the values provided by the PLC to the virtual system in MATLAB. Furthermore, the lack of physical components in the virtual testbed such as the PLC does not allow to run it along with the physical testbed. Furthermore, the virtual testbed is limited to one simulated attack which is a change of setpoint. The results obtained from the experimentation phase show that the hybrid testbed shows a similar operation to the physical testbed. The CWSS-V testbed can provide insights about the operation of the system under normal conditions, but under attack, the results are uncertain and limited given that the implementation of novel attacks is almost impossible. For example, the attacks on the PLC memory, like the ones described in this paper, cannot be executed in a virtual environment.

Research Question 2. Can we rely on mechanisms of anomaly detection on ICS which are developed and tested on virtual platforms?

The comparison of the physical, hybrid, and virtual testbeds, shown in this paper, demonstrate that each testbed has a different behaviour when a cyber-attack occurs. The virtual testbed has a notable limitation when it is compared with the rest of the testbeds. For instance, the novel set of attacks against the PLC memory described in this paper cannot be implemented in a virtual environment because it does not implement a physical PLC. Thus, we can argue that the mechanisms of attack detection developed in virtual environments might not be accurate at detecting cyber-attacks when they are deployed in physical environments.

5.2. Testbed Comparison

Table 2 provides a summary of the testbeds described in the related work and the testbeds implemented in this research. The physical testbeds provided by the authors [6,7,8,9] which are related to the physical testbed implemented in our research, operate with the protocol Modbus TCP which is known for having a considerable number of vulnerabilities [36,37]. Thus, the impact of cyber-attacks to critical infrastructures that operate with Modbus protocol has been extensively explored. In this research, we propose a more realistic set of attacks that can occur in a real scenario, those attacks target the Siemens PLC memory with the aim of overwriting it. Unlike attacks like Man-In-The-Middle, Dos, ARP Spoofing, which are used in related work and have been widely explored in different investigations.

Table 2. ICS testbeds for cyber-security research.

	Type	Components	Network Protocol	Attack Vector
CWSS: Clean Water Supply System (our research)	Physical	PLC, SCADA, HMI	Profinet, TCP/IP	Packet Crafting, PLC memory corruption
SWaT: six-stage water treatment process [7]	Physical	PLCs, HMIs, SCADA, RTUs, Wireless Sensors	CIP over Ethernet/IP, Ethernet/IP	Man-In-The-Middle, ARP Spoofing
FACIES: water distribution system [8]	Physical	PLCs, SCADA.	TCP/IP, Modbus/TCP	ARP Spoofing, Man-In-The-Middle
WADI: A Water Distribution Testbed for Research [6]	Physical	PLC, HMI, RTUs, SCADA	Ethernet	Packet delay variation, variable packet loss
Water treatment process [9]	Physical	PLC, SCADA-HMI	Modbus, Profinet	Unclear
HITL Testbed: Tennessee Eastman (TE) chemical process [11]	Hybrid	Process modelled in MATLAB. Physical PLC, SCADA, RTIB, SIB	Serial-Interface Board	ARP Spoofing, False Data Injection
CWSS-H: Hybrid Clean Water Supply System (our research)	Hybrid	Process modelled in MATLAB. Physical PLC. OPC Server.	TCP/IP	Packet Crafting, PLC memory corruption
HEDVa: Hybrid Environment for Design and Validation [12]	Hybrid	Uses an agent-based grid simulation model. Real PLC and SCADA.	Modbus TCP/IP	ARP Spoofing, Man In The Middle
Hybrid implementation of a water distribution system [14]	Hybrid	PLC, RTU, two tanks, virtual plant	Modbus TCP/IP	DoS, ARP Spoofing
VTET: A Virtual Industrial Control System Testbed for Cyber Security Research [13]	Virtual Hybrid	Virtual PLC, PC, Physical PLC.	OPC-S7-Modbus TCP/IP	DoS Attack
Water purification plant [18]	Virtual	PLC, HMI, a virtual tank, heater, two valves, level and temperature sensor	Modbus TCP	Man-In-The-Middle, reconnaissance attacks
Water Distribution System [15]	Virtual	Virtual Machines: RTU, MTU, HMI	Modbus TCP	DoS Attack, ARP Spoofing
TASSCS: A Testbed for analysing security of SCADA control systems [19]	Virtual	HMI, PLC, three virtual water tanks	Modbus	Man-In-The-Middle, DoS
SCADAVT-A Framework for building SCADA [16]	Virtual	Three computers: HMI, PG, IED.	IEC 60870-5	Man-In-The-Middle, ARP Spoofing
CWSS-V: Virtual Clean Water Supply System (our research)	Virtual	Process fully modelled in MATLAB including PID controller.	NA	False Data Injection

The hybrid testbeds implemented in related works [11,12,13,14] also lack the implementation of a novel set of attacks employed during the validation tests, while in our research we still implement the set of attacks targeting the PLC memory. Furthermore, our virtual process implemented in MATLAB is composed of sensors and actuators with the same properties as physical sensors and actuators. In addition, during the creation of the virtual process, the performance of the physical and virtual process was compared during the different stages of the implementation. It is worth mentioning that it is not clear if the virtual processes implemented in the related work are implemented based on their physical counterpart.

The virtual testbed implemented in this research uses the same virtual process employed by the hybrid testbed. The main difference lays in the set of attacks used against the control process. It can be determined that cybersecurity research in virtual testbeds does not allow to have a real perspective of the impact that cyber-attacks have on control processes. For this reason, it is advisable to use real control processes implemented with physical equipment, thus, it is possible to determine the impact of cyber-attacks.

6. Conclusions

This paper compares a physical, hybrid, and virtual testbed operation from a cybersecurity perspective. Under normal operation the physical and hybrid testbeds show similar behaviour; however, their behaviour is different when they are under attack. Furthermore, the virtual testbed shows many limitations when implementing the attack scenarios. For this testbed, it is difficult to replicate attacks to the input memory of the PLC, although, it is feasible to modify the setpoint. The mathematical equation obtained from the physical system serves only to show a representation of the control process, however, it can be argued whether a security system such as an IDS can be built based on the represented mathematical equation.

The cyber-attack detection mechanisms in ICS require a comprehensive understanding of the system operation. Achieving this knowledge through the information obtained from virtual simulation environments is complex and often impossible. The physical dynamics of the components such as sensors and actuators cannot be simulated in a virtual environment. Therefore, in our point of view, it is unrealistic and rather unsafe to rely on detection mechanisms created in virtual environments. According to the results obtained during the experimentation phase, the physical environments allow us to visualise the behaviour of cyber-attacks in a real ICS with the aim of providing an accurate and efficient mechanism of cyber-attack detection.