SYSTEM AND METHOD FOR CONTROLLING MOLTEN SALT TEMPERATURE
    1.
    发明申请
    SYSTEM AND METHOD FOR CONTROLLING MOLTEN SALT TEMPERATURE 有权
    控制盐水温度的系统和方法

    公开(公告)号:US20150128931A1

    公开(公告)日:2015-05-14

    申请号:US14074782

    申请日:2013-11-08

    Abstract: The molten salt solar tower system 100 is provided for controlling molten salt temperature in a solar receiver 130 for effective operation of the system 100 while without degrading physical properties of molten salt. The system 100 includes two circuits, first 140 and second 150. The first circuit 140 is configured to supply relatively cold molten salt in the solar receiver 130 for heating, and the second circuit 150 is configured to supply a predetermined amount of the relatively cold molten salt in the first circuit 140, as and when the temperature of the relatively hot molten salt circulating through the solar receiver 130 exceeds a predetermined set temperature value thereof.

    Abstract translation: 提供熔盐太阳能塔系统100用于控制太阳能接收器130中的熔融盐温度,以有效地操作系统100,同时不降低熔融盐的物理性能。 系统100包括两个电路,第一电路140和第二电路150.第一电路140被配置为在太阳能接收器130中提供相对冷的熔融盐,用于加热,而第二电路150构造成提供预定量的相对冷的熔融 当通过太阳能接收器130循环的相对热的熔融盐的温度超过其预定的设定温度值时,第一回路140中的盐。

    MODEL-BASED CONTROLS FOR A FURNACE AND METHOD FOR CONTROLLING THE FURNACE
    2.
    发明申请
    MODEL-BASED CONTROLS FOR A FURNACE AND METHOD FOR CONTROLLING THE FURNACE 审中-公开
    基于模型的控制炉和控制炉的方法

    公开(公告)号:US20160209031A1

    公开(公告)日:2016-07-21

    申请号:US14600804

    申请日:2015-01-20

    Abstract: Disclosed herein is a control system for NOx reduction in a power plant, the control system comprising a model predictive controller; a proportional integral differential controller and/or an adaptive controller; where the proportional integral differential controller and/or an adaptive controller are subordinated to and in operative communication with the model predictive controller; where the proportional integral differential controller and/or an adaptive controller comprise a feedback loop; a NOx reduction system comprising a NOx reducing agent supply tank and a water supply tank; and a furnace for combusting a fuel; where the furnace lies downstream of the NOx reduction system and where the furnace is provided with a plurality of nozzles that are in fluid communication with the NOx reduction system; where the control system is in electrical communication with the NOx reduction system.

    Abstract translation: 本发明公开了一种用于发电厂NOx还原的控制系统,该控制系统包括模型预测控制器; 比例积分微分控制器和/或自适应控制器; 其中比例积分微分控制器和/或自适应控制器从属于模型预测控制器并与模型预测控制器进行操作性通信; 其中比例积分微分控制器和/或自适应控制器包括反馈回路; 包括NOx还原剂供应罐和供水箱的NOx还原系统; 和燃烧燃料的炉子; 其中所述炉位于所述NOx还原系统的下游,并且所述炉子设置有与所述NOx还原系统流体连通的多个喷嘴; 其中控制系统与NOx还原系统电连通。

    NONLINEAR MODEL PREDICTIVE CONTROL FOR CHEMICAL LOOPING PROCESS
    3.
    发明申请
    NONLINEAR MODEL PREDICTIVE CONTROL FOR CHEMICAL LOOPING PROCESS 有权
    化学循环过程的非线性模型预测控制

    公开(公告)号:US20140025210A1

    公开(公告)日:2014-01-23

    申请号:US13946115

    申请日:2013-07-19

    CPC classification number: G05D7/0617 G05B13/042 G05B17/02

    Abstract: A control system for optimizing a chemical looping (“CL”) plant includes a reduced order mathematical model (“ROM”) that is designed by eliminating mathematical terms that have minimal effect on the outcome. A non-linear optimizer provides various inputs to the ROM and monitors the outputs to determine the optimum inputs that are then provided to the CL plant. An estimator estimates the values of various internal state variables of the CL plant. The system has one structure adapted to control a CL plant that only provides pressure measurements in the CL loops A and B, a second structure adapted to a CL plant that provides pressure measurements and solid levels in both loops A, and B, and a third structure adapted to control a CL plant that provides full information on internal state variables. A final structure provides a neural network NMPC controller to control operation of loops A and B.

    Abstract translation: 用于优化化学循环(“CL”)设备的控制系统包括通过消除对结果具有最小影响的数学术语而设计的简化数学模型(“ROM”)。 非线性优化器向ROM提供各种输入并监视输出以确定然后提供给CL工厂的最佳输入。 估计器估计CL工厂的各种内部状态变量的值。 该系统具有适于控制仅在CL循环A和B中提供压力测量的CL设备的一种结构,适于CL设备的第二结构,其在环A和B中提供压力测量和固体水平,以及第三结构 结构适用于控制提供关于内部状态变量的完整信息的CL工厂。 最终结构提供神经网络NMPC控制器来控制环路A和B的操作。

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