CINECA IRIS Institutional Research Information System

SCALI, CLAUDIO
 Distribuzione geografica
Salva come PNG Salva come JPEG
Continente #
NA - Nord America 11.030
AS - Asia 5.534
EU - Europa 5.495
SA - Sud America 585
AF - Africa 340
OC - Oceania 8
Continente sconosciuto - Info sul continente non disponibili 1
Totale 22.993
Salva come PNG Salva come JPEG
Nazione #
US - Stati Uniti d'America 10.474
CN - Cina 2.066
IT - Italia 1.978
SG - Singapore 1.572
SE - Svezia 964
HK - Hong Kong 855
DE - Germania 542
BR - Brasile 520
CA - Canada 491
KR - Corea 468
UA - Ucraina 433
BG - Bulgaria 404
GB - Regno Unito 308
FI - Finlandia 195
VN - Vietnam 189
TR - Turchia 188
CH - Svizzera 178
PL - Polonia 163
RU - Federazione Russa 156
CI - Costa d'Avorio 155
NG - Nigeria 100
IN - India 55
MX - Messico 45
FR - Francia 41
SN - Senegal 37
BE - Belgio 33
BD - Bangladesh 24
NL - Olanda 24
IQ - Iraq 22
ES - Italia 21
AR - Argentina 17
JP - Giappone 15
BJ - Benin 12
IE - Irlanda 12
CL - Cile 11
ZA - Sudafrica 11
CZ - Repubblica Ceca 10
IR - Iran 10
VE - Venezuela 10
CO - Colombia 8
ID - Indonesia 8
EC - Ecuador 7
MA - Marocco 7
MY - Malesia 6
PK - Pakistan 6
TW - Taiwan 6
AL - Albania 5
AU - Australia 5
CR - Costa Rica 5
GR - Grecia 5
JO - Giordania 5
LT - Lituania 5
TH - Thailandia 5
TN - Tunisia 5
UY - Uruguay 5
AE - Emirati Arabi Uniti 4
IL - Israele 4
JM - Giamaica 4
KE - Kenya 4
PE - Perù 4
AT - Austria 3
AZ - Azerbaigian 3
LK - Sri Lanka 3
NZ - Nuova Zelanda 3
PA - Panama 3
PH - Filippine 3
RS - Serbia 3
UZ - Uzbekistan 3
BO - Bolivia 2
DK - Danimarca 2
DO - Repubblica Dominicana 2
EG - Egitto 2
LU - Lussemburgo 2
NP - Nepal 2
OM - Oman 2
PS - Palestinian Territory 2
AF - Afghanistan, Repubblica islamica di 1
AM - Armenia 1
AO - Angola 1
BB - Barbados 1
BH - Bahrain 1
BY - Bielorussia 1
CD - Congo 1
DM - Dominica 1
DZ - Algeria 1
EE - Estonia 1
EU - Europa 1
GA - Gabon 1
GE - Georgia 1
GT - Guatemala 1
HU - Ungheria 1
IS - Islanda 1
KG - Kirghizistan 1
KZ - Kazakistan 1
LA - Repubblica Popolare Democratica del Laos 1
MG - Madagascar 1
ML - Mali 1
NO - Norvegia 1
PT - Portogallo 1
PY - Paraguay 1
Totale 22.986
Salva come PNG Salva come JPEG
Città #
Ann Arbor 1.178
Woodbridge 1.148
Ashburn 909
Hong Kong 851
Singapore 848
Houston 765
Chandler 744
Milan 701
Fairfield 680
Hefei 626
Jacksonville 590
Santa Clara 528
Seoul 464
Sofia 402
Dallas 365
Beijing 309
Shanghai 300
Munich 296
Seattle 281
New York 269
Wilmington 266
Ottawa 259
Cambridge 240
Mcallen 211
Montréal 211
Boardman 176
Bern 175
Nanjing 173
Princeton 171
Lawrence 156
Abidjan 155
Serra 120
Florence 117
Des Moines 115
Jüchen 108
Izmir 103
Dearborn 100
Lagos 99
Los Angeles 99
Medford 92
Buffalo 68
Istanbul 65
Dong Ket 64
Nanchang 62
Council Bluffs 57
Kunming 55
Rome 51
São Paulo 45
Livorno 41
Redondo Beach 40
Redwood City 38
Dakar 37
Boulder 35
Chicago 34
Ogden 32
San Diego 30
Brussels 28
Shenyang 27
Tianjin 27
London 24
Changsha 22
Hebei 20
Jiaxing 20
Norwalk 19
Columbus 18
Amsterdam 16
Ho Chi Minh City 16
The Dalles 16
Washington 16
Guangzhou 15
Hangzhou 15
Pisa 15
San Jose 15
Verona 15
Baghdad 14
Pune 13
Belo Horizonte 12
Cotonou 12
Hanoi 12
Dhaka 11
Orange 11
Tokyo 11
Turku 11
Auburn Hills 10
Brasília 10
Campinas 10
Curitiba 10
Massa 10
Paris 10
Brooklyn 9
Lanzhou 9
Padova 9
Chengdu 8
Dublin 8
Fortaleza 8
Frankfurt am Main 8
Mexico City 8
Phoenix 8
Recife 8
Rio de Janeiro 8
Totale 16.756
Salva come PNG Salva come JPEG
Nome #
Ecco come ‘Industria 4.0’ migliora l’industria di processo (Il Monitoraggio delle Prestazioni degli Impianti nello Scenario dell’Industria 4.0) 350
Non linear standard regulators 349
A Comparison of Techniques for Automatic Detection of Stiction: Simulation and Application to Industrial Data 346
null 312
An augmented PID control structure to compensate for valve stiction 301
ROBUST TUNING OF CONVENTIONAL CONTROLLERS 249
Numerical investigation of the mixing of highly viscous liquids with Cowles impellers 241
null 237
A Two-Phase flow model for Geothermal Wells in the Presence of Non-Condensable Gas 237
Improved Qualitative Shape Analysis Technique for Automatic Detection of Valve Stiction in Flow Control loops 234
A Characterization of Oscillating Phenomena on Sieve Plates of Transfer Columns 220
A New Performance Evaluation Strategy for Decentralized Multivariable PID Control Systems 210
Variable structure PI controllers in the presence of uncertainty and saturation 206
Tuning of Conventional Controllers for Robust Performance 203
A METHOD FOR ROBUST TUNING OF LINEAR-QUADRATIC OPTIMAL CONTROLLERS 199
Biomethane Production: Mass and Energy Balances of Alternative Supply Chains 199
Analysis of operating conditions of autoaccelerating batch reactors 197
System identification applied to stiction quantification in industrial control loops: A comparative study 196
Enhancing MPC formulations by identification and estimation of valve stiction 195
Control of the Quality of Polymer Products in Continuous Reactors: Comparison of Performance of State Estimators with and without Updating of Parameters 194
PERFORMANCE OF DIFFERENT REGULATORS FOR PLANTS WITH RECYCLE 193
Identification techniques for stiction quantification in the presence of nonstationary disturbances 191
An Application of Lyapounov's Methods for Batch Reactors Stability Studies 185
FEEDFORWARD CONTROL IN THE PRESENCE OF UNCERTAINTY 181
Controller Design for a Multiproduct Distillation Unit in the Presence of Uncertainty 179
Identification and estimation of valve stiction by the use of a smoothed model 179
Issues in the Control of Systems with Recycle 176
Issues in on-line Implementation of a Closed Loop Performance System 176
DESIGN OF DOUBLE FILTER IMC CONTROLLER FOR ILL-CONDITIONED DISTILLATION-COLUMNS 174
Optimal operation strategies to control the molecular weight distribution of polymer products 172
Design and Control Selections for Cascade Loops in Distillation 172
Performance of Control Scheme Based on Estimators in the Control of Continuous Polymerization Reactors 169
COMPARISON OF INTERNAL MODEL CONTROL AND LINEAR QUADRATIC OPTIMAL-CONTROL FOR SISO SYSTEMS 168
Control of Systems with Recycle by means of Compensators 168
Analisi di Schemi di Controllo in Cascata per Processi Chimici 166
Controllability Analysis by Plant Oriented Techniques: Application to the Tennessee Eastman Benchmark 166
Robustness Issues in Feedforward Control 165
Variable Structure Regulators for Industrial Process Control 165
Performance of Optimal and Standard Controllers for Disturbance Rejection in Industrial Processes 164
Algoritmi di Controllo per Regolatori di Processo Non Lineari 163
Modeling the Prediction of the Effect of the Molecular Weight Distribution of Polymer Products 161
Process control performance evaluation in the case of variable set-point with experimental applications 161
Automatic Detection of Stiction in Actuators: A Technique to Reduce the Number of Uncertain Cases. 160
Performance of control systems based on recycle compensators in integrated plants 157
Control of Overshoot in the Step Response of Chemical Processes 157
Improved Identification and Autotuning of PI Controllers for MIMO Processes by Relay Techniques 156
Temperature Oscillation Calorimetry: Robustness Analysis of Different Algorithms for the Evaluation of the Heat Transfer Coefficient 156
Analysis and Design of Cascade Control Schemes in Distillation 155
Adaptive Control of an Experimental Distillation Column by Relay Methods 154
Preface to Special Issue on Process Control 154
Selection and Tuning of Decentralized Systems for Chemical Processes 153
Dynamics and Control of Chemical Plants with Recycle Streams 153
Comportamento Dinamico e Controllo di un Impianto di Prova per Pompe di Calore 152
Implementation, Parameters Calibration and Field Validation of a Closed Loop Performance Monitoring System 152
A Revised Technique of Stiction Compensation for Control Valves 152
A Data-Base Measure for Interactions in Multivariate Systems 151
Accuracy of Autotuning Identification Methods and Achievable Closed Loop Performance 151
Modelling of Polymerization Reactors: the Influence of Diffusion Phenomena on the Choice of Operating Conditions 149
Analisi di Schemi di Doppio Controllo di Composizione per Colonne di Distillazione 148
A comparison of Relay Techniques for Identification and Autotuning of Chemical Processes 148
null 147
Analisi di Strategie di Controllo per Colonne Termicamente Integrate 147
Nitrificazione e Bilancio di Ossigeno nelle Acque Correnti 146
Multiloop Autotuning Using Relay Feedback: Limits and Extensions 145
Closed Loop Performance Monitoring: Automatic Diagnosis of Valve Stiction by means of a Technique based on Shape Analysis Formalism 145
OPTIMIZATION OF BATCH POLYMERIZATION REACTORS - MODELING AND EXPERIMENTAL RESULTS FOR SUSPENSION POLYMERIZATION OF METHYLMETHACRYLATE 144
Analysis of Molecular Weight Distribution in Free Radical Polymerization 143
Analytical Design of PID Controllers for Inverse Response Processes 142
Relay with Additional Delay for Identification and Autotuning of Completely Unknown Processes 142
Use of Modified Relay Techniques for the Design of Model Based Controllers for Chemical Processes 141
Relay Autotuning of Multivariable systems: Application to an Experimental Pilot-Scale Distillation Column 141
Identification of Chemical Processes for Control Purposes by Relay Techniques 140
Controllo della Emissione di Idrogeno Solforato da Bacini di Trattamento di Acque di Scarico 139
Comparative performance analysis of an electric actuator for control valves 139
Selection of Control Configurations for the Tennessee Eastman Benchmark 138
A Method for Determining an Optimal Temperature Profile for Molecular Weight Distribution Control 135
Analysis of Parametric Sensitivity of Optimal Temperature Profiles in Batch Polymerization 135
Parameter Extimation in Extended Kalman Filters for Quality Control in Polymerization Reactors 135
Modeling Disturbance Dynamics to Improve Controller Performance in Industrial Loops 135
Controlling Ill-Conditioned Plants: SISO Controllers in Distillation 134
Control of Polymerization Reactors using State Estimators with Different Time Scales 133
Analysis of Molecular Weight Distribution in Polymerization Processes 133
Identification of Unknown Processes for Autotune Purposes by Relay Tests 133
A Cloud-Based Monitoring System for Performance Assessment of Industrial Plants 133
Study of Diffusion Controlled Polymerization through the Analysis of the Molecular Weight Distribution 132
Evaluation of Time Varying Parameters in Polymerization Reactors by means of Temperature Oscillation Calorimetry 132
Sequential versus Simultaneous Relay Techniques for Autotuning of Multivariable Processes 132
Performance improvements of cascade and feed-forward control schemes for industrial processes 131
An Industry 4.0 demonstrator for cloud-based performance monitoring and assessment of industrial plants 131
Identification and Control of Open Loop Unstable Processes by Relay Methods 130
Autotuning of PI controllers via Relay with Hysteresys 126
Automatic Diagnosis of Valve Stiction by means of a Qualitative Shape Analysis Technique 126
Sequential Identification and Autotuning by Relay Techniques of Decentralised Controllers for Multivariable Chemical Processes 125
Design of Decentralized Controllers by a Relay Technique: Extension of Tuning Rules 123
Closed-Loop Identification and Control of Multivariable Chemical Processes: a Case Study 123
Soluzione di Problemi di Interazione nel Controllo di Colonne di Distillazione mediante Disaccoppiamento Implicito 122
Tecniche di Riconciliazione Dati nella Ottimizzazione dei Processi: Applicazione ad una Caldaia di Potenza 119
null 119
Control of Polymerization Reactors by Means of Different State Estimators 118
"Adattamento in Linea di Regolatori PID per Reattori di Polimerizzazione in Condizioni Operative Instabili" 116
Totale 16.777
Salva come PNG Salva come JPEG
Categoria #
all - tutte 55.902
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 55.902
Salva come PNG Salva come JPEG


Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2020/2021869 0 0 0 0 0 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
2024/20254.492 36 193 71 203 384 340 404 311 409 601 785 755
2025/20262.793 304 869 531 314 310 465 0 0 0 0 0 0
Totale 23.161