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    Some other methods of controlling have been imposed
    on this process and have gained acceptable answers but
    fuzzy PID control and fuzzy control have been imposed
    rarely.
    Khaksar et al. [44] used a fuzzy self-tuning PID con-
    troller for temperature control of mentioned process and
    showed that its performance is better than classic PID
    controller.
    In this section, we consider temperature control problem
    of a CSTR in which an unstable first-order exothermic
    reaction takes place. A fuzzy PID controller is used in this
    section.
    4.2 Modeling equations
    Consider a CSTR in which an exothermic first-order
    reaction takes place (A ? B). The material and energy
    balances based on the assumptions of constant volume
    inside the reactor, perfect mixing and constant physical
    properties allow obtaining the dynamic model. The
    differential equations can be written in dimensionless form
    as follows [41].where x1,x2,x3, and qc are the dimensionless concentra-
    tion, reactor temperature, cooling-jacket temperature, and
    cooling-jacket flow rate, respectively. The main objective
    is controlling the reactor temperature with manipulating the
    coolant flow rate (qc). The values of the parameters are
    given in Table 5.
    CSTR exhibits ignition/extinction behavior for this set
    of parameters. Here, we study the system at two operating
    points, one unstable (Op1) and one stable (Op2).
    The unsteady-state values of the three states and of the
    manipulated input are (Op1):
    x1s ¼ 0:4737; x2s ¼ 3:1702; x3s ¼0:2968; qcs
    ¼ 1:482225
    The high-temperature steady state (Op2) is open loop stable
    with the following steady-state values [44, 45]:
    x1s ¼ 0:2028; x2s ¼ 5; x3s ¼ 0:4079; qcs ¼ 0:97854.3 Simulation results
    In this section, trial-and-error method is used to find the
    controller parameters of classic PID. Afterward, these
    parameters are optimized and resulted parameters are
    shown in the Table 6.
    In fuzzy PID, fuzzy tuner must calculate the controller
    parameters. This tuner has two inputs: error e(t) and
    derivative of error d(t), and three outputs: Kp, Ki and Kd.
    For the input and output variables (e,de, Kp, Ki, and Kd),
    five membership functions Z, VS, S, M, and B are used.
    They are Z, zero; VS, very small; S, small; M, medium;
    and B, big. The triangle membership function for inputs
    and outputs is shown in Fig. 7.
    The fuzzy inference rules are shown in Table 7.The proposed fuzzy PID-type controller has been com-
    pared with the classic PID controller. The closed loop
    responses of CSTR are shown in Fig. 8.
    The results show that the fuzzy PID controller has better
    performance than PID controller.
    5 pH control system
    pH control is vital in some processes and design of it must
    be accurate for these processes [46, 47]. Different methods
    have been investigated for designing of linear and nonlin-
    ear pH processes control in different papers; for instance,
    control of total model [48], control of inner model [49],
    control of same reactions, and fuzzy PI control in basis of
    scheduled gain [50–53].
    Regarding high nonlinearity of pH process, performance
    of classic PID controller is inappropriate and we must find
    better controllers such as fuzzy controller and predictive
    controller for pH process.
    Most of the research on pH control in last 2 decades are
    about using fuzzy controller or combining of it with con-
    trollers on basis of model prediction [54–56]. In another
    work [48], there is a review on controller’s types that
    imposed to pH neutralization process.
    According to the papers on pH neutralization process
    control, fuzzy PID controller is a relatively appropriate
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