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In process systems, analysis of control degrees of freedom (CDOF) is a primary step for control structure design.
Spans of control, degrees of job enlargement, forms of decentralization, planning systems, and matrix structure should not be picked and chosen at random.
Also, we provide a theoretical justification for existing empirical arguments concerning the loss of control degrees of freedom caused by process intensification.
The focus of this paper is on one of the important steps in designing plant-wide control systems, namely, control degrees of freedom (CDOF).
First, three different HIDiC structures, i.e. an ideal HIDiC, a HIDiC with a pre-heater, and a HIDiC with a reboiler, are analyzed by control degrees of freedom (DOF).
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When the concrete drying process stars from water saturation, there is little difference between the control degree of cathodic reaction and the control degree of anodic reaction on corrosion process; the control type of corrosion reaction is mixed control.
The incorporation of a second control degree of freedom, the propeller pitch angle, makes it possible to meet all the control objectives.
These posture selection results are consistent with the concept of controlling degrees of freedom most relevant to task performance [43], [44].
Living radical polymerization with "iniferter" (initiator-transfer agent-terminator) is useful tool for controlling degree of polymerization by reaction time.
First infilling well density was 54.4 wells/km2, reserves' controlled degree of water flooding was 83.2 %; the second infilling well density was 86.7 wells/km2, reserves' controlled degree of water flooding was 93.1 %; in 2007, when the water cut of block was 92.5 %, the third infilling well pattern density was 134 wells/km2, reserves' controlled degree of water flooding was 97.3 %.
For example, the well pattern density and the producer injector ratio are indexes with casual relationship with the reserves' controlled degree of water flooding.
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