CINECA IRIS Institutional Research Information System

SCALI, CLAUDIO
 Distribuzione geografica
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Continente #
NA - Nord America 8.881
EU - Europa 5.160
AS - Asia 1.352
AF - Africa 294
SA - Sud America 28
OC - Oceania 7
Continente sconosciuto - Info sul continente non disponibili 1
Totale 15.723
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Nazione #
US - Stati Uniti d'America 8.378
IT - Italia 1.931
SE - Svezia 958
CN - Cina 772
DE - Germania 505
CA - Canada 473
UA - Ucraina 420
BG - Bulgaria 401
GB - Regno Unito 292
SG - Singapore 204
CH - Svizzera 176
FI - Finlandia 176
VN - Vietnam 158
PL - Polonia 155
CI - Costa d'Avorio 154
TR - Turchia 109
NG - Nigeria 99
SN - Senegal 37
HK - Hong Kong 33
FR - Francia 31
BE - Belgio 29
RU - Federazione Russa 26
IN - India 25
MX - Messico 24
ES - Italia 14
IE - Irlanda 12
BR - Brasile 11
IQ - Iraq 10
CZ - Repubblica Ceca 8
IR - Iran 8
NL - Olanda 7
CL - Cile 6
GR - Grecia 5
ID - Indonesia 5
AU - Australia 4
CR - Costa Rica 4
KR - Corea 4
TW - Taiwan 4
VE - Venezuela 4
AR - Argentina 3
CO - Colombia 3
IL - Israele 3
JP - Giappone 3
MY - Malesia 3
NZ - Nuova Zelanda 3
PH - Filippine 3
RS - Serbia 3
TH - Thailandia 3
AT - Austria 2
PA - Panama 2
ZA - Sudafrica 2
AE - Emirati Arabi Uniti 1
AF - Afghanistan, Repubblica islamica di 1
AL - Albania 1
BH - Bahrain 1
DK - Danimarca 1
EE - Estonia 1
EU - Europa 1
HU - Ungheria 1
IS - Islanda 1
LA - Repubblica Popolare Democratica del Laos 1
LK - Sri Lanka 1
ML - Mali 1
NO - Norvegia 1
PT - Portogallo 1
RO - Romania 1
SC - Seychelles 1
SK - Slovacchia (Repubblica Slovacca) 1
UY - Uruguay 1
Totale 15.723
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Città #
Ann Arbor 1.178
Woodbridge 1.148
Houston 761
Chandler 744
Milan 694
Fairfield 680
Jacksonville 590
Sofia 401
Ashburn 391
Seattle 280
Munich 273
Wilmington 266
Ottawa 257
Beijing 256
New York 255
Cambridge 240
Mcallen 211
Montréal 211
Bern 175
Nanjing 173
Princeton 171
Lawrence 156
Abidjan 154
Serra 120
Des Moines 115
Florence 115
Jüchen 108
Izmir 103
Dearborn 100
Lagos 98
Medford 92
Singapore 71
Dong Ket 64
Nanchang 62
Kunming 53
Rome 43
Livorno 41
Redwood City 38
Dakar 37
Boulder 35
Ogden 32
Hong Kong 31
San Diego 30
Shenyang 26
Tianjin 26
Brussels 25
Changsha 22
Hefei 22
Chicago 20
Hebei 20
Jiaxing 20
London 19
Norwalk 19
Washington 16
Boardman 15
Verona 15
Los Angeles 14
Pisa 14
Pune 12
Guangzhou 11
Orange 11
Auburn Hills 10
Hangzhou 10
Massa 10
Shanghai 10
Lanzhou 9
Padova 9
Baghdad 8
Dublin 8
Alessandria 7
Monsummano Terme 7
Chengdu 6
Indiana 6
Phoenix 6
Changchun 5
Hanoi 5
Mexico City 5
Warangal 5
Chongqing 4
Council Bluffs 4
Córdoba 4
Drogheda 4
Duncan 4
Edinburgh 4
Frankfurt am Main 4
Jinan 4
León 4
Messina 4
Monte Argentario 4
Nürnberg 4
Paris 4
Tappahannock 4
Bari 3
Bologna 3
Carrara 3
Chihuahua 3
Como 3
Falls Church 3
Hyderabad 3
Kilburn 3
Totale 11.586
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Nome #
null 312
A Comparison of Techniques for Automatic Detection of Stiction: Simulation and Application to Industrial Data 293
Ecco come ‘Industria 4.0’ migliora l’industria di processo (Il Monitoraggio delle Prestazioni degli Impianti nello Scenario dell’Industria 4.0) 289
Non linear standard regulators 276
An augmented PID control structure to compensate for valve stiction 245
null 237
Improved Qualitative Shape Analysis Technique for Automatic Detection of Valve Stiction in Flow Control loops 201
ROBUST TUNING OF CONVENTIONAL CONTROLLERS 182
A New Performance Evaluation Strategy for Decentralized Multivariable PID Control Systems 173
A Two-Phase flow model for Geothermal Wells in the Presence of Non-Condensable Gas 165
A Characterization of Oscillating Phenomena on Sieve Plates of Transfer Columns 160
Tuning of Conventional Controllers for Robust Performance 148
null 147
System identification applied to stiction quantification in industrial control loops: A comparative study 147
Variable structure PI controllers in the presence of uncertainty and saturation 146
PERFORMANCE OF DIFFERENT REGULATORS FOR PLANTS WITH RECYCLE 145
A METHOD FOR ROBUST TUNING OF LINEAR-QUADRATIC OPTIMAL CONTROLLERS 145
Biomethane Production: Mass and Energy Balances of Alternative Supply Chains 141
Analysis of operating conditions of autoaccelerating batch reactors 138
Control of the Quality of Polymer Products in Continuous Reactors: Comparison of Performance of State Estimators with and without Updating of Parameters 137
Identification techniques for stiction quantification in the presence of nonstationary disturbances 135
Numerical investigation of the mixing of highly viscous liquids with Cowles impellers 135
Enhancing MPC formulations by identification and estimation of valve stiction 132
Issues in on-line Implementation of a Closed Loop Performance System 129
DESIGN OF DOUBLE FILTER IMC CONTROLLER FOR ILL-CONDITIONED DISTILLATION-COLUMNS 127
Control of Overshoot in the Step Response of Chemical Processes 127
Performance of control systems based on recycle compensators in integrated plants 126
An Application of Lyapounov's Methods for Batch Reactors Stability Studies 125
FEEDFORWARD CONTROL IN THE PRESENCE OF UNCERTAINTY 124
Design and Control Selections for Cascade Loops in Distillation 124
Controllability Analysis by Plant Oriented Techniques: Application to the Tennessee Eastman Benchmark 124
Identification and estimation of valve stiction by the use of a smoothed model 124
Controller Design for a Multiproduct Distillation Unit in the Presence of Uncertainty 119
Issues in the Control of Systems with Recycle 119
null 119
Automatic Detection of Stiction in Actuators: A Technique to Reduce the Number of Uncertain Cases. 118
Accuracy of Autotuning Identification Methods and Achievable Closed Loop Performance 118
Robustness Issues in Feedforward Control 117
Performance of Optimal and Standard Controllers for Disturbance Rejection in Industrial Processes 116
Modeling the Prediction of the Effect of the Molecular Weight Distribution of Polymer Products 113
Process control performance evaluation in the case of variable set-point with experimental applications 113
Variable Structure Regulators for Industrial Process Control 112
Control of Systems with Recycle by means of Compensators 112
A Data-Base Measure for Interactions in Multivariate Systems 112
null 112
Implementation, Parameters Calibration and Field Validation of a Closed Loop Performance Monitoring System 112
Preface to Special Issue on Process Control 110
A comparison of Relay Techniques for Identification and Autotuning of Chemical Processes 110
Identification of Chemical Processes for Control Purposes by Relay Techniques 109
Relay Autotuning of Multivariable systems: Application to an Experimental Pilot-Scale Distillation Column 109
Performance of Control Scheme Based on Estimators in the Control of Continuous Polymerization Reactors 108
Adaptive Control of an Experimental Distillation Column by Relay Methods 108
Use of Modified Relay Techniques for the Design of Model Based Controllers for Chemical Processes 108
Optimal operation strategies to control the molecular weight distribution of polymer products 107
Closed Loop Performance Monitoring: Automatic Diagnosis of Valve Stiction by means of a Technique based on Shape Analysis Formalism 107
Relay with Additional Delay for Identification and Autotuning of Completely Unknown Processes 106
Temperature Oscillation Calorimetry: Robustness Analysis of Different Algorithms for the Evaluation of the Heat Transfer Coefficient 105
Improved Identification and Autotuning of PI Controllers for MIMO Processes by Relay Techniques 104
null 103
A Revised Technique of Stiction Compensation for Control Valves 102
Selection and Tuning of Decentralized Systems for Chemical Processes 101
Modeling Disturbance Dynamics to Improve Controller Performance in Industrial Loops 100
Analysis of Molecular Weight Distribution in Free Radical Polymerization 99
Dynamics and Control of Chemical Plants with Recycle Streams 98
Analysis and Design of Cascade Control Schemes in Distillation 97
Sequential versus Simultaneous Relay Techniques for Autotuning of Multivariable Processes 97
Modelling of Polymerization Reactors: the Influence of Diffusion Phenomena on the Choice of Operating Conditions 95
Analisi di Schemi di Controllo in Cascata per Processi Chimici 94
Multiloop Autotuning Using Relay Feedback: Limits and Extensions 94
null 93
Comportamento Dinamico e Controllo di un Impianto di Prova per Pompe di Calore 92
Analisi di Schemi di Doppio Controllo di Composizione per Colonne di Distillazione 91
Controllo della Emissione di Idrogeno Solforato da Bacini di Trattamento di Acque di Scarico 89
A Method for Determining an Optimal Temperature Profile for Molecular Weight Distribution Control 89
Analytical Design of PID Controllers for Inverse Response Processes 89
Closed-Loop Identification and Control of Multivariable Chemical Processes: a Case Study 89
Comparative performance analysis of an electric actuator for control valves 89
Algoritmi di Controllo per Regolatori di Processo Non Lineari 88
Automatic Diagnosis of Valve Stiction by means of a Qualitative Shape Analysis Technique 88
A Cloud-Based Monitoring System for Performance Assessment of Industrial Plants 88
Selection of Control Configurations for the Tennessee Eastman Benchmark 87
Evaluation of Time Varying Parameters in Polymerization Reactors by means of Temperature Oscillation Calorimetry 87
Analisi di Strategie di Controllo per Colonne Termicamente Integrate 86
Nitrificazione e Bilancio di Ossigeno nelle Acque Correnti 86
Identification and Control of Open Loop Unstable Processes by Relay Methods 86
Performance improvements of cascade and feed-forward control schemes for industrial processes 86
COMPARISON OF INTERNAL MODEL CONTROL AND LINEAR QUADRATIC OPTIMAL-CONTROL FOR SISO SYSTEMS 84
Study of Diffusion Controlled Polymerization through the Analysis of the Molecular Weight Distribution 84
Analysis of Parametric Sensitivity of Optimal Temperature Profiles in Batch Polymerization 84
Identification of Unknown Processes for Autotune Purposes by Relay Tests 83
Sequential Identification and Autotuning by Relay Techniques of Decentralised Controllers for Multivariable Chemical Processes 83
OPTIMIZATION OF BATCH POLYMERIZATION REACTORS - MODELING AND EXPERIMENTAL RESULTS FOR SUSPENSION POLYMERIZATION OF METHYLMETHACRYLATE 81
Design of Decentralized Controllers by a Relay Technique: Extension of Tuning Rules 81
Control of Polymerization Reactors using State Estimators with Different Time Scales 79
Analysis of Molecular Weight Distribution in Polymerization Processes 79
null 79
Controlling Ill-Conditioned Plants: SISO Controllers in Distillation 78
null 78
Parameter Extimation in Extended Kalman Filters for Quality Control in Polymerization Reactors 76
An Automatic System for Closed Loop Performance Monitoring 76
Totale 11.970
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Categoria #
all - tutte 34.349
article - articoli 0
book - libri 0
conference - conferenze 0
curatela - curatele 0
other - altro 0
patent - brevetti 0
selected - selezionate 0
volume - volumi 0
Totale 34.349
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2019/20202.934 292 246 100 170 280 237 261 183 409 296 327 133
2020/20211.762 230 142 208 114 199 61 205 118 84 133 65 203
2021/20221.665 13 125 32 158 357 215 39 81 96 72 60 417
2022/20232.302 293 263 130 191 321 301 32 154 396 12 193 16
2023/20242.324 369 277 350 176 309 311 55 35 78 168 42 154
2024/202515 15 0 0 0 0 0 0 0 0 0 0 0
Totale 15.891