Exact(2)
Responses of serum HBV DNA and ALT were categorized into three groups according to degree of response to lamivudine treatment: continuous, unstable, and no response.
All of these patients experienced corneal damage and symptoms of continuous unstable corneal curvature (CUCC).
Similar(58)
This inequality shows that the initial-condition-to-solution map (R_{beta}), (beta< infty), also is continuous at unstable equilibria.
Let us consider the following continuous-time unstable plant: dot{boldsymbol{x}}_{mathrm{c}}(t) = A_{mathrm{c}}boldsymbol{x}_{mathrm{c}}(t) + boldsymbol{b}_{mathrm{c}}u_{mathrm{c}}(t), with A_{mathrm{c}} = left[begin{array}{ccc} 3&-1.5&0.5 3&-1.5&0.5 2&0&0 0&1&0right],quad boldsymbol{b}_{mathrm{c}} = lend{array}right]{c} 0.5 0 0 end{array}right].
In this work, the problem of controlling (possibly open-loop unstable) continuous free-radical solution polymer reactors with continuous measurements of temperature, level and flows, and discrete-delayed measurements of molecular weight (MW) is addressed.
The control of unstable continuous stirred tank reactors for emulsion polymerization is addressed.
This paper describes application of nonlinear long range predictive control to an open loop unstable continuous stirred tank reactor.
The start-up of an open-loop unstable continuous free-radical homopolymerization reactor is considered as an application example.
The robust feedforward (FF) output-feedback (OF) control problem of (possibly open-loop unstable) continuous exothermic jacketed reactors with isotonic kinetics with respect to reactant concentration is considered.
The main features of the new control algorithm are illustrated through an example of the temperature control of an open-loop unstable continuous stirred tank reactor.
The problem of controlling (possibly open-loop unstable) continuous free-radical solution polymer reactors with temperature, level and flow measurements is addressed.
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