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      <title>controlguru.com is an e-textbook on best practices and proven methods for automatic process control</title>
      <link>http://www.controlguru.com/</link>
      <description>Proven Methods and Best Practices for PID Process Control</description>
      <language>en-us</language>
      <pubDate>Sun, 04 May 2008 00:00:01 EST</pubDate>
      <managingEditor>doug.cooper@controlguru.com</managingEditor>
      <webMaster>doug.cooper@controlguru.com</webMaster>
      <item>
         <title>The Feed Forward Controller (by Doug Cooper and Allen Houtz)</title>
         <link>http://www.controlguru.com/2008/050408.html</link>
         <description>A feed forward controller receives a measured disturbance signal, uses it to predict an impact on the 
	 process variable, and then computes preemptive control actions that counteract the predicted impact as the 
         disturbance arrives to maintain the process variable at set point (PV = SP) throughout the disturbance          event.</description>
         <pubDate>Sun, 04 May 2008 00:00:01 EST</pubDate>
      </item>
     <item>
         <title>Ratio with Cross-Limiting Override Control of a Combustion Process (by Allen Houtz and Doug Cooper)</title>
         <link>http://www.controlguru.com/2008/041308.html</link>
         <description>Here we explore the addition of a second select override element to create a 
         cross-limiting architecture that prevents the air/fuel ratio fed to the burner from becoming overly 
         rich (too much fuel) or lean (too much air) as operating conditions change. Variations on this 
         cross-limiting architecture are widely employed within the air/fuel ratio logic of a broad range 
         of industrial combustion control systems.</description>
         <pubDate>Sun, 13 Apr 2008 00:00:01 EST</pubDate>
     </item>
     <item>
         <title>Override (Select) Elements and Their Use in Ratio Control (by Allen Houtz and Doug Cooper)</title>
         <link>http://www.controlguru.com/2008/030908.html</link>
         <description>A select element enables decision-making logic to be included in a control strategy, 
          which in turn provides a means for increasing strategy sophistication. A popular application explored in 
          this article is to use a select override in a ratio control architecture. In particular, we explore how a 
          select override can be included in an air/fuel ratio combustion control strategy to enhance safety, 
          limit emissions and maximize useful energy from fuel.</description>
         <pubDate>Sun, 09 Mar 2008 00:00:01 EST</pubDate>
     </item>
     <item>
         <title>Integral (Reset) Windup, Jacketing Logic and the Velocity PI Form (by Doug Cooper)</title>
         <link>http://www.controlguru.com/2008/021008.html</link>
         <description>A valve cannot open more than all the way. A pump cannot go slower than stopped. Yet 
          an improperly programmed control algorithm can issue such commands. Herein lies the problem of 
          integral windup (also referred to as reset windup or integral saturation). It is a problem that 
          has been around for decades and was solved long ago. We discuss why it occurs and how to prevent 
          it to help those who choose to write their own control algorithm.</description>
         <pubDate>Sun, 10 Feb 2008 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>Ratio Control and Metered-Air Combustion Processes (by Allen Houtz and Doug Cooper)</title>
         <link>http://www.controlguru.com/2008/012708.html</link>
         <description>A ratio control strategy can play a fundamental role in the safe and profitable operation of 
          fired heaters, boilers, furnaces and similar fuel burning processes. This is because the air-to-fuel ratio 
          in the combustion zone of these processes directly impacts fuel combustion efficiency and environmental emissions.
          A requirement for ratio control implementation is that both the fuel feed rate and combustion air feed rate 
          are measured and available as process variable signals.</description>
         <pubDate>Sun, 27 Jan 2008 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>The Ratio Control Architecture (by Allen Houtz and Doug Cooper)</title>
         <link>http://www.controlguru.com/2007/120207.html</link>
         <description>The ratio control architecture is used to maintain the flow rate of one stream 
          in a process at a defined or specified proportion relative to that of another. A common 
          application for ratio control is to combine or blend two feed streams to produce a mixed 
          flow with a desired composition or physical property.</description>
         <pubDate>Sun, 02 Dec 2007 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>Controller Gain Is Dimensionless in Commercial Systems (by Doug Cooper)</title>
         <link>http://www.controlguru.com/2007/110407.html</link>
         <description>Like most control room displays, the Controlguru.com e-book presents PV values 
         in engineering units. These are used directly in tuning correlations 
         to compute controller gains, Kc. As a result, the Kc values also carry engineering units.
         The benefit of this approach is that Kc maintains the intuitive familiarity 
         that engineering units provide. The difficulty is that commercial controllers are normally 
         configured to use a dimensionless values. This article explores how to convert a Kc with 
         engineering units into the standard dimensionless (%/%) form.</description>
         <pubDate>Sun, 04 Nov 2007 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>An Implementation Recipe for Cascade Control (by Doug Cooper)</title>
         <link>http://www.controlguru.com/2007/090207.html</link>
         <description>When improved disturbance rejection is our goal, one benefit of  
         cascade control over a feed forward strategy is that implementing a cascade builds upon our 
         existing skills. A cascade has two controllers, and the proecedure is a familiar task because 
         it essentially is to employ our controller design and tuning recipe twice in sequence.</description>
         <pubDate>Sun, 2 Sep 2007 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>The Cascade Control Architecture (by Doug Cooper)</title>
         <link>http://www.controlguru.com/2007/070607.html</link>
         <description>Cascade control is an architecture 
         capable of reducing the impact of disturbances on our measured process 
         variable (PV). To construct a cascade architecture, we literally nest a secondary control loop 
         inside a primary loop as shown in the block diagram.</description>
         <pubDate>Fri, 6 Jul 2007 00:00:01 EST</pubDate>
      </item>
      <item>
         <title>PI Control of the Integrating Pumped Tank Process (by Bob Rice and Doug Cooper)</title>
         <link>http://www.controlguru.com/2007/042507.html</link>
         <description>The control objective for the pumped tank process is to maintain liquid level 
         at set point by adjusting the discharge flow rate out of the bottom of the tank. This 
         process displays the distinctive integrating (or non-self regulating) behavior, and as such, 
         presents an interesting control challenge. </description>
         <pubDate>Wed, 25 Apr 2007 00:00:01 EST</pubDate>
      </item>
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