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    • 1. 发明授权
    • Optimizing plant control values of a power plant
    • 优化发电厂的工厂控制值
    • US07058552B2
    • 2006-06-06
    • US10021344
    • 2001-12-19
    • Alec StothertEduardo Gallestey AlvarezMarkus AhrensMarc AntoineSteve Morton
    • Alec StothertEduardo Gallestey AlvarezMarkus AhrensMarc AntoineSteve Morton
    • G06F17/10G06G7/48G05B13/02
    • G05B13/042
    • In a method and computer program product for optimizing power plant control values and a power plant optimizing system an optimization module (1) minimizes total plant operation costs while achieving predetermined required output values for produced power and process steam. This is done by, at a given time, determining future values of control values and simulating, in a simulation module (2), the behavior of the plant up to a given future time. Corresponding fuel costs and generated power are determined in the simulation, and incorporated in an objective function. The optimization module (1) minimizes the objective function by varying the control values. According to the invention, a rate of ageing of plant components is determined when simulating the future behavior of the plant, and the objective function to be minimized comprises said rate of ageing.
    • 在用于优化发电厂控制值的方法和计算机程序产品以及发电厂优化系统中,优化模块(1)最小化总设备运行成本,同时实现产生的功率和过程蒸汽的预定的所需输出值。 这通过在给定时间确定控制值的未来值并在模拟模块(2))中模拟工厂在给定未来时间的行为来完成。 相应的燃料成本和发电量在模拟中确定,并入目标函数。 优化模块(1)通过改变控制值来最小化目标函数。 根据本发明,在模拟植物的未来行为时确定植物组分的老化速率,并且要最小化的目标函数包括所述衰老速率。
    • 2. 发明授权
    • Optimal operation of a power plant
    • 发电厂的最佳运行
    • US07426456B2
    • 2008-09-16
    • US10298573
    • 2002-11-19
    • Eduardo Gallestey AlvarezAlec StothertMarc AntoineSteve Morton
    • Eduardo Gallestey AlvarezAlec StothertMarc AntoineSteve Morton
    • G06F17/10
    • G05B19/41885G05B2219/32017G05B2219/32343Y02E20/16Y02P90/26Y02P90/86
    • In a method and computer program product for optimal operation of a power plant and a power plant optimising system an optimisation mode (1) minimises a cost function (J[u],J[P]) that comprises a deviation of lifetime of plant components (LTp(τ)) from a desired nominal lifetime trajectory (LTn(τ)). This is done by, at a given time, determining future values of input values (u(τ),P(τ)) such as control values (P(τ)) or process values (u(τ)) to the plant and simulating, in a simulation modulate (2), the behaviour of the plant up to a given future time. Corresponding lifetime values are determined in the simulation, and incorporated in an objective function. The optimisation module (1) minimises the cost function (J[u],J[P]) by varying the input values (u(τ),P(τ)). As a result, it is possible to operate the plant such that component lifetime (LTp(τ)) follows the desired trajectory (LTn(τ)).
    • 在用于发电厂和发电厂优化系统的最佳运行的方法和计算机程序产品中,优化模式(1)使包括工厂部件的寿命偏差的成本函数(J [u],J [P])最小化 (LTp(τ))从期望的标称寿命轨迹(LTn(τ))。 这通过在给定时间来确定植物的输入值(u(τ),P(τ))的未来值(例如控制值(P(τ))或过程值(u(τ))) 模拟,在模拟调制(2)中,植物的行为直到给定的未来时间。 相应的寿命值在模拟中确定,并入目标函数。 优化模块(1)通过改变输入值(u(τ),P(τ))来最小化成本函数(J [u],J [P])。 因此,可以使设备操作,使得组件寿命(LTp(τ))遵循期望的轨迹(LTn(τ))。
    • 3. 发明申请
    • METHOD AND SYSTEM FOR CONTROLLING AN INDUSTRIAL PROCESS
    • 控制工业过程的方法和系统
    • US20110208341A1
    • 2011-08-25
    • US13051249
    • 2011-03-18
    • Konrad STADLEREduardo Gallestey AlvarezJan Poland
    • Konrad STADLEREduardo Gallestey AlvarezJan Poland
    • G06F19/00
    • G05B13/0275G05B13/04
    • A control system for controlling an industrial process includes an indicator generator configured to determine at least one fuzzy logic based indicator from measured process variables. The control system also includes a state estimator configured to determine estimated physical process states based on the fuzzy indicator. For controlling the industrial process, the process controller is configured to calculate manipulated variables based on (i) defined set-points and (ii) a physical model of the process using the estimated physical process states. Combining a fuzzy logic indicator with a model based process controller provides robust indicators of the process states for controlling an industrial process in a real plant situation in which measured process variables may possibly contradict each other.
    • 用于控制工业过程的控制系统包括指示器发生器,其被配置为从测量的过程变量确定至少一个基于模糊逻辑的指示符。 控制系统还包括状态估计器,其被配置为基于模糊指示器来确定估计的物理过程状态。 为了控制工业过程,过程控制器被配置为基于(i)定义的设定点和(ii)使用估计的物理过程状态的过程的物理模型来计算操纵变量。 将模糊逻辑指示器与基于模型的过程控制器相结合,为测量过程变量可能相互矛盾的实际工厂情况中控制工业过程提供了强大的过程状态指标。