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    • 42. 发明申请
    • Cascaded control of an average value of a process parameter to a desired value
    • US20060058899A1
    • 2006-03-16
    • US10926991
    • 2004-08-27
    • Scott BoydenStephen Piche
    • Scott BoydenStephen Piche
    • G05B13/02
    • G05B13/026B01D53/30B01D2257/302B01D2257/404G05B13/021
    • A multi-tier controller directs operation of a system performing a process. The process has multiple process parameters (MPPs), at least one of the MPPs being a controllable process parameter (CTPP) and one of the MPPs being a targeted process parameter (TPP). The process also has a defined target limit (DTV) representing a first limit on an actual average value (MV) of the TPP over a defined time period of length TPLAAV2. The AAV is computed based on actual values (AVs) of the TPP over the defined period. A first logical controller predicts future average values (FAVs) of the TPP over a first future time period (FFTP) having a length of at least TPLAAV2 and extending from a current time T0 to an future time TAAV2, prior to which the TPP will move to steady state. The FAVs are predicted based on (i) the AAVs of the TPP at various times over a first prior time period (FPTP) having a length of at least TPLAAV2 and extending from a prior time of T-AAV2 to the current time T0, (ii) the current values of the MPPs, and (iii) the DTV. A second logical controller establishes a further target limit (FTV) representing a second limit on the MV of the TPP for a second future time period (SFTP) having a length equal to TPLAAV2, which is less than the length TPLAAV2, and extending from the current time T0 to a future time TAAV1. The FTV is established based on one or more of the predicted FAVs of the TPP over the FFTP. The second logical controller also determines a target set point for each CTPP based on (i) the AAVs of the TPP at various times over a second prior time period (SPTP) having the length TPLAAV1 and extending from a prior time T-AAV1 to the current time T0, (ii) the current values of the MPPs, and (iii) the FTV. The second logical controller additionally has logic to direct control of each CTPP in accordance with the determined target set point for that CTPP.
    • 46. 发明授权
    • APC process parameter estimation
    • APC过程参数估计
    • US08197753B2
    • 2012-06-12
    • US12917985
    • 2010-11-02
    • Scott A. BoydenStephen Piche
    • Scott A. BoydenStephen Piche
    • B01D53/60B01D53/56B01D53/54B01D53/34G05B23/02
    • G05B13/027B01D2257/302B01D2257/404G05B13/048Y10T436/12
    • A virtual analyzer is provided to estimate either an attribute of a reactant applied during performance of, or an amount of a reactant exhausted by, a process having multiple process parameters (MPPs) that is performed to control an amount of a pollutant emitted into the air. The virtual analyzer includes an interface which receives signals corresponding to attributes of the MPPs. If the process is a wet flue gas desulfurization (WFGD) process, the signals include a signal corresponding to a measured pH level of the applied reactant. If the process is a selective catalytic reduction (SCR) process, the signals include a signal corresponding to a measured amount of the reactant exhausted by the process.
    • 提供虚拟分析器以估计在执行过程中施加的反应物的属性,或由具有多个处理参数(MPP)的过程所排出的反应物的量的属性,所述过程参数(MPP)被执行以控制排放到空气中的污染物的量 。 虚拟分析器包括接收与MPP的属性对应的信号的接口。 如果该方法是湿式烟道气脱硫(WFGD)方法,信号包括对应于施加的反应物的测量的pH值的信号。 如果该方法是选择性催化还原(SCR)方法,信号包括对应于由该方法排出的反应物的测量量的信号。
    • 47. 发明授权
    • System for optimizing power generating unit
    • 优化发电机组的系统
    • US08068923B2
    • 2011-11-29
    • US12916773
    • 2010-11-01
    • Stephen Piche
    • Stephen Piche
    • G05D3/12G05B13/02
    • H02J3/38F23N2023/40F23N2023/44H02J2003/007Y02E40/76Y02E60/76Y04S10/545Y04S40/22
    • A method and apparatus for optimizing the operation of a single or multiple power generating units using advanced optimization, modeling, and control techniques. In one embodiment, a plurality of component optimization systems for optimizing power generating unit components are sequentially coordinated to allow optimized values determined by a first component optimization system to be fed forward for use as an input value to a subsequent component optimization system. A unit optimization system may be provided to determine goals and constraints for the plurality of component optimization systems in accordance with economic data. In one embodiment of the invention, a multi-unit optimization system is provided to determine goals and constraints for component optimization systems of different power generating units. Both steady state and dynamic models are used for optimization.
    • 一种使用先进优化,建模和控制技术优化单个或多个发电机组的运行的方法和装置。 在一个实施例中,用于优化功率产生单元组件的多个组件优化系统被顺序地协调,以允许由第一组件优化系统确定的优化值被提前向用作后续组件优化系统的输入值。 可以提供单元优化系统以根据经济数据确定多个部件优化系统的目标和约束。 在本发明的一个实施例中,提供多单元优化系统以确定不同发电单元的部件优化系统的目标和约束。 稳态和动态模型均用于优化。
    • 48. 发明授权
    • Cost based control of air pollution control
    • 空气污染控制成本控制
    • US07634417B2
    • 2009-12-15
    • US10927049
    • 2004-08-27
    • Scott A. BoydenStephen Piche
    • Scott A. BoydenStephen Piche
    • G06Q10/00
    • G06Q10/06B01D53/346B01D53/504G06Q30/0283G06Q40/00
    • A controller for directing operation of an air pollution control (APC) system, requires a consumable to perform a process to control emissions of a pollutant. The process has multiple process parameters (MPPs). One or more of the MPPs is a controllable process parameters (CTPPs) and one of the MPPs is an amount of the pollutant (AOP) emitted by the system. A defined AOP value (AOPV) represents a limit on an actual value (AV) of the emitted AOP. An interface receives a value corresponding to a unit cost of the consumable. A control processor determines the cost of operating the system based on the received value corresponding to the unit cost of the consumable, and directs control of at least one of CTPPs based on the current value of that CTPP and the determined operating cost.
    • 用于指挥空气污染控制(APC)系统运行的控制器需要耗材来执行控制污染物排放的过程。 该过程具有多个过程参数(MPP)。 一个或多个MPP是可控制的过程参数(CTPP),其中一个MPP是系统发射的污染物(AOP)的量。 定义的AOP值(AOPV)表示发射的AOP的实际值(AV)的限制。 接口接收与消耗品的单位成本相对应的值。 控制处理器基于与消耗品的单位成本对应的接收值来确定操作系统的成本,并且基于该CTPP的当前值和所确定的运行成本来指导至少一个CTPP的控制。
    • 49. 发明授权
    • Model based sequential optimization of a single or multiple power generating units
    • 单个或多个发电机组的基于模型的顺序优化
    • US07599750B2
    • 2009-10-06
    • US11314214
    • 2005-12-21
    • Stephen Piche
    • Stephen Piche
    • G05D3/12G05B13/02
    • H02J3/38F23N2023/40F23N2023/44H02J2003/007Y02E40/76Y02E60/76Y04S10/545Y04S40/22
    • A method and apparatus for optimizing the operation of a single or multiple power generating units using advanced optimization, modeling, and control techniques. In one embodiment, a plurality of component optimization systems for optimizing power generating unit components are sequentially coordinated to allow optimized values determined by a first component optimization system to be fed forward for use as an input value to a subsequent component optimization system. A unit optimization system may be provided to determine goals and constraints for the plurality of component optimization systems in accordance with economic data. In one embodiment of the invention, a multi-unit optimization system is provided to determine goals and constraints for component optimization systems of different power generating units. Both steady state and dynamic models are used for optimization.
    • 一种使用先进优化,建模和控制技术优化单个或多个发电机组的运行的方法和装置。 在一个实施例中,用于优化功率产生单元组件的多个组件优化系统被顺序地协调,以允许由第一组件优化系统确定的优化值被提前向用作后续组件优化系统的输入值。 可以提供单元优化系统以根据经济数据确定多个部件优化系统的目标和约束。 在本发明的一个实施例中,提供多单元优化系统以确定不同发电单元的部件优化系统的目标和约束。 稳态和动态模型均用于优化。