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Donald R Semrad

age ~64

from Madison, WI

Also known as:
  • Donald J Semrad
  • Don J Semrad

Donald Semrad Phones & Addresses

  • Madison, WI
  • Tomahawk, WI
  • Richardson, TX
  • 2319 Little Elm Trl, Cedar Park, TX 78613 • 512 794-1107
  • Mc Kinney, TX
  • Austin, TX
  • Pardeeville, WI
  • 8810 Timber Wolf Trl, Madison, WI 53717 • 608 824-0905

Education

  • Degree:
    Graduate or professional degree

Emails

Us Patents

  • Method For Optimizing A Plant With Multiple Inputs

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  • US Patent:
    6381504, Apr 30, 2002
  • Filed:
    Dec 31, 1998
  • Appl. No.:
    09/224648
  • Inventors:
    John P. Havener - Austin TX
    Stephen Piche - Austin TX
    Donald Semrad - Cedar Park TX
    Brian K. Stephenson - Round Rock TX
  • Assignee:
    Pavilion Technologies, Inc. - Austin TX
  • International Classification:
    G05B 1302
  • US Classification:
    700 44, 700 28, 700 34
  • Abstract:
    An on-line optimizer is provided wherein a boiler (720) is optimized by measuring a select plurality of inputs to the boiler (720) and mapping them through a predetermined relationship that defines a single value representing a spacial relationship in the boiler that is a function of the select inputs. This single value is then optimized with the use of a plant optimizer (818) which provides an optimized value. This optimized value is then processed thought the inverse relationship of the single modified value to provide modified inputs to the plant that can be applied to the plant.
  • Method For Optimizing A Plant With Multiple Inputs

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  • US Patent:
    6950711, Sep 27, 2005
  • Filed:
    Feb 25, 2002
  • Appl. No.:
    10/082783
  • Inventors:
    John P. Havener - Austin TX, US
    Stephen Piche - Austin TX, US
    Donald Semrad - Cedar Park TX, US
    Brian K. Stephenson - Round Rock TX, US
  • Assignee:
    Pavilion Technologies - Austin TX
  • International Classification:
    G06F019/00
  • US Classification:
    700 28, 700 45, 702181, 219497
  • Abstract:
    An on-line optimizer is provided wherein a boiler () is optimized by measuring a select plurality of inputs to the boiler () and mapping them through a predetermined relationship that defines a single value representing a spacial relationship in the boiler that is a function of the select inputs. This single value is then optimized with the use of a plant optimizer () which provides an optimized value. This optimized value is then processed thought the inverse relationship of the single modified value to provide modified inputs to the plant that can be applied to the plant.
  • Method For Optimizing A Plant With Multiple Inputs

    view source
  • US Patent:
    20030014131, Jan 16, 2003
  • Filed:
    Jan 8, 2002
  • Appl. No.:
    10/041769
  • Inventors:
    John Havener - Austin TX, US
    Stephen Piche - Austin TX, US
    Donald Semrad - Cedar Park TX, US
    Brian Stephenson - Round Rock TX, US
  • International Classification:
    G05B013/02
  • US Classification:
    700/029000, 700/028000
  • Abstract:
    An on-line optimizer is provided wherein a boiler () is optimized by measuring a select plurality of inputs to the boiler () and mapping them through a predetermined relationship that defines a single value representing a spacial relationship in the boiler that is a function of the select inputs. This single value is then optimized with the use of a plant optimizer () which provides an optimized value. This optimized value is then processed thought the inverse relationship of the single modified value to provide modified inputs to the plant that can be applied to the plant.
  • Method For On-Line Optimization Of A Plant

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  • US Patent:
    6278899, Aug 21, 2001
  • Filed:
    Oct 6, 1998
  • Appl. No.:
    9/167504
  • Inventors:
    Stephen Piche - Austin TX
    John P. Havener - Austin TX
    Donald Semrad - Cedar Park TX
  • Assignee:
    Pavilion Technologies, Inc. - Austin TX
  • International Classification:
    G05B 1302
  • US Classification:
    700 44
  • Abstract:
    An on-line optimizer is comprised of a nonlinear dynamic model (702) which is operable to provide an estimation of the output of a plant. This receives manipulated variables (MV), disturbance variables (DV), and computed disturbance variables (CDB). The estimated output of the model is then compared to the actual output measured by virtual on-line analyzer (VOA) (616). This is compared is a difference block 618 to generate a bias which is then filtered by a filter(620). The output thereof is then provided to an output block (672) in a steady state optimizer (700) to offset the desired setpoints. These set points are input to a steady state nonlinear model which is operable to optimize the inputs to the plants for use for writing new set points in accordance with a predetermined cost function. This cost function is utilized to optimize the new inputs with the use of the steady state model in accordance with various constraints and target values.

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