Åbo akademi. Institutionen för reglerteknik. Report

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• Åbo Akademi. Institutionen för reglerteknik

hasPart

• 1970-1980 : 10 år reglerteknik vid Åbo akademi = 10 years process control at Åbo akademi
• 1[sub 1]-identification toolbox for Matlab
• A bicriterion stationary LQ control problem
• A capacitive analyzer for ethanol-water mixtures : Part 1, An oscillator for measuring the capacitance of the cell
• A combined internal model and inferential control structure for distillation
• A comparison of six control approaches for two-product control of distillation
• A computer aided design procedure for multiobjective LQG control problems
• A disturbance sensitivity parameter for evaluation of distillation control performance
• A linear dynamic programming application to a production-transportation control model
• A model structure for capturing the process directionality in non-ideal distillation
• A preliminary study of a model-based control structure for two-point control of distillation
• A program package for parametric LQ problems
• A robust H[sub 2] performance problem for discrete-time systems
• A robust H[sub 2] performance problem for uncertain plants
• A self-tuning controller for systems with non-square transfer functions
• A self-tuning regulator based on optimal output feedback theory
• A self-tuning regulator with on-line cost function adaptation
• A simulation study of a class of algorithms for adaptive pH control
• A simulation study of multivariable control and estimation strategies for chemical engineering processes
• A study of modeling and control of pH in fast acid-base reaction processes based on chemical reaction invariance
• A study of the dynamics of calcium-phosphate precipitation in pH-control systems
• A trade-off minimax linear quadratic control problem
• A two-channel relay for autotuning
• Adaptive methods for linear and nonlinear control of pH
• An experimental comparison of four control structures for two-point control of distillation
• Analytical relationships between frequency-dependent relative gains for distillation control structures
• Analytical relative gain expressions for distillation control structures
• Application of chemical reaction invariants in modeling and control of ph
• Application of stochastic control theory to the dry cement manufacturing process
• Approximation and identification of continuous-time system
• Approximation of delay systems : a case study
• Approximative modelling of systems : approximation complexity
• Automatic re-tuning of PI controllers in oscillating control loops
• Autotuning of multiloop control systems
• Calculation of the pH value of a mixture of solutions : an illustration of the use of chemical reaction invariants
• Chemical reaction invariants in modeling and control of pH
• Combined internal model and inferential control of a distillation column via closed-loop identification
• Consistent control structure modeling with application to distillation control
• Constrained linear quadratic gaussian control for process application
• Conventional and model based control of a mixing tank
• Design and tuning of dual-composition distillation control system by the inverse Nyquist array method
• Destillationsanläggningen vid Institutionen för reglerteknik vid Åbo akademi
• Discretization of analog filters via H[sub ääretön] model matching theory
• Distillation control structures for simultaneous disturbance rejection and implicit decoupling
• Distillation control structures, consistency and transformations
• Distillation dynamics and multivariable control : selected papers 1971-1983 from the Process Control Laboratory at Åbo akademi
• Disturbance rejection properties of control structures at one-point control of a two-product distillation column
• EFA : an expert system for elementary feasibility analysis
• En introduktion till Siman på PC
• Estimation of consistent process gains for distillation control structures
• Ett övningsexempel i stokastisk processreglering
• Ett övningsexempel i stokastisk processreglering
• Evaluating distillation control structures
• Exact linearization techniques for process control : a review and some examples
• Experimental comparison of distillation control structures
• Fundamental properties of continuous pH control
• H[sub ∞] control of multirate sampled-data systems : a state-space approach
• Identification of stabilizable systems : closed-loop approximation
• Indirect two-point control through one-point control of distillation
• Introduction to interval methods in automatic control
• Investigation of a finite memory observer structure
• Knowledge based simulation systems : a survey
• Laguerre series approximation of infinite dimensional systems
• Linear quadratic design of structure-constrained controllers
• Minimax robust LQ control of a thermomechanical pulping plant
• Mixed H[sub 2]/H[sub omega] control : synthesis equations for the discrete-time case
• Mixed H[sub 2]/H[sub omega] control of sampled-data systems
• Model reduction by Laguerre filters
• Modeling and identification of the low-gain direction of ill-conditioned plants
• Modeling of distillation control structures
• Modelling of uncertain systems via linear programming
• Multimodel robust control of nonlinear plants : a case study
• Multiple control criteria and optimal control
• Multiple models, multiplicative noise and linear quadratic control : algorithmic aspects
• Multivariable gain identification for process control
• Multivariable nonlinear and adaptive control of a distillation column
• Multivariable self-tuning PID control of a distillation column
• Multivariable self-tuning PID control of a mixing tank
• Myths about pH and pH control
• Nonlinear and adaptive control of pH
• Några kommentarer till "The dominant eigenvalue method"
• On bounded error identification of feedback systems
• On H[sup infinity] identification of stable systems and optimal approximation
• On l[sup 1] approximation and identification of discrete-time systems
• On Laguerre methods and H[sup infinity] identification of continuous-time systems
• On minimax linear quadratic control
• On Newton's method for variance-constrained optimal output feedback problems
• On numerical methods for parametric LQ problems
• On optimal stochastic control theory in process control
• On sensor fault detection and isolation in dynamic systems
• On steady-state multiplicity in binary distillation
• On stochastic control theory and self-tuning regulators with applications to process control
• On the difference between distillation column control structures
• On the H[sub ääretön]-type smoothing problem
• On using sums and differences to control distillation
• On worst-case identification of continuous-time systems
• Oscillations in feedback systems for pH control
• Parametrization of a disturbance rejecting and decoupling control structure
• Pascal for the RTZ80 : design considerations
• Pascal for the RTZ80 : implementation
• Pascal for the RTZ80 : users manual
• Proof of the relation between principal directions and flow gains in distillation
• PROXIM : an interactiv system for process control simulation
• Reconciliation of process gains for distillation control structures
• Robust approximation and identification in H[sup ääretön]
• Robust discrete approximation and worst-case identification
• Robust identification and Galois sequences
• Robust multiobjective LQ control of distillation using low-order controllers
• Robust recursive identification : the eigenvalue tracking method
• Robust stabilization : BIBO stability, distance notions and robustness optimization
• Robustness and dynamic design of disturbance rejecting and decoupling control structures
• Sampled-data control of continuous-time systems with an H[sub ääretön] optimality criterion
• Sampled-data H[sub ääretön] optimal control of time-varying systems
• Sampling prefilters with an H[sub ääretön] criterion
• Self-tuning regulators for process control
• Simple models for distillation dynamics
• Some iterative methods in linear dynamic programming
• Some simple facts a chemical engineer should know about stochastic control
• Some topics in adaptive pH control
• State estimation in multivariable PI-control
• The sampled-data H[omega] problem : a unified framework for discretization based methods and Riccati-equation solution
• Three approaches toward a fault-tolerant controller structure
• Transformations and consistency relations of distillation control structures : 1, Theory
• Transformations and consistency relations of distillation control structures : 2, Applications
• Transformations between distillation control structures
• Worst-case identification of feedback systems from closed-loop time series
• Worst-case input-output identification
• Åbo akademis pilot-plant destillationskolonn och dess reglersystem

inLanguage

• en
• sv

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• Fennica

issn

• 0357-7228

name

• Rapport / Åbo Akademi, kemisk-tekniska fakulteten, institutionen för reglerteknik
• Rapport / Åbo akademi. Kemisk-tekniska fakulteten. Institutionen för reglerteknik
• Rep. - Åbo Akad., Kem.-tek. fak., Inst. reglertek
• Report
• Report / Åbo Akademi, Department of Chemical Engineering, Process Control Laboratory
• Report / Åbo Akademi, Kemisk-tekniska fakulteten, Institutionen för reglerteknik
• Report / Åbo Akademi, kemisk-tekniska fakulteten, institutionen för reglerteknik
• Report / Åbo akademi. Institutionen för reglerteknik
• Report / Åbo akademi. Kemisk-tekniska fakulteten. Institutionen för reglerteknik
• Report / Åbo Akademi. Kemisk-tekniska fakulteten. Institutionen för reglerteknik
• Report / Åbo akademi. Kemisk-teknista fakulteten. Institutionen för reglerteknik
• Åbo akademi. Institutionen för reglerteknik. Report
• Åbo akademi. Kemisk-tekniska fakulteten. Institutionen för reglerteknik. Report
• ��bo akademi. Institutionen för reglerteknik. Report

P60049

• <http://rdaregistry.info/termList/RDAContentType/1020>

sameAs

• <https://issn.org/resource/issn/0357-7228>

Instances

• 1978-1997 : Åbo Akademi