CINECA IRIS Institutional Research Information System

SCALI, CLAUDIO
 Distribuzione geografica
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Continente #
NA - Nord America 9.975
EU - Europa 5.368
AS - Asia 2.536
AF - Africa 319
SA - Sud America 206
OC - Oceania 7
Continente sconosciuto - Info sul continente non disponibili 1
Totale 18.412
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Nazione #
US - Stati Uniti d'America 9.457
IT - Italia 1.961
CN - Cina 1.124
SE - Svezia 958
SG - Singapore 727
DE - Germania 519
CA - Canada 480
UA - Ucraina 428
BG - Bulgaria 402
GB - Regno Unito 293
HK - Hong Kong 244
FI - Finlandia 181
TR - Turchia 178
CH - Svizzera 176
BR - Brasile 172
VN - Vietnam 159
PL - Polonia 155
CI - Costa d'Avorio 154
RU - Federazione Russa 147
NG - Nigeria 99
SN - Senegal 37
BE - Belgio 33
FR - Francia 31
IN - India 30
MX - Messico 29
NL - Olanda 22
IQ - Iraq 17
ES - Italia 14
BJ - Benin 12
IE - Irlanda 12
CZ - Repubblica Ceca 10
AR - Argentina 8
CL - Cile 8
IR - Iran 8
CO - Colombia 6
TW - Taiwan 6
VE - Venezuela 6
CR - Costa Rica 5
GR - Grecia 5
ID - Indonesia 5
ZA - Sudafrica 5
AU - Australia 4
IL - Israele 4
KR - Corea 4
MA - Marocco 4
AL - Albania 3
AT - Austria 3
EC - Ecuador 3
JP - Giappone 3
MY - Malesia 3
NZ - Nuova Zelanda 3
PA - Panama 3
PH - Filippine 3
RS - Serbia 3
TH - Thailandia 3
TN - Tunisia 3
AE - Emirati Arabi Uniti 2
BD - Bangladesh 2
JO - Giordania 2
LT - Lituania 2
LU - Lussemburgo 2
PK - Pakistan 2
AF - Afghanistan, Repubblica islamica di 1
AM - Armenia 1
AO - Angola 1
AZ - Azerbaigian 1
BH - Bahrain 1
DK - Danimarca 1
DZ - Algeria 1
EE - Estonia 1
EU - Europa 1
GE - Georgia 1
HU - Ungheria 1
IS - Islanda 1
JM - Giamaica 1
KE - Kenya 1
LA - Repubblica Popolare Democratica del Laos 1
LK - Sri Lanka 1
ML - Mali 1
NO - Norvegia 1
NP - Nepal 1
OM - Oman 1
PE - Perù 1
PT - Portogallo 1
PY - Paraguay 1
RO - Romania 1
SC - Seychelles 1
SK - Slovacchia (Repubblica Slovacca) 1
UY - Uruguay 1
UZ - Uzbekistan 1
Totale 18.412
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Città #
Ann Arbor 1.178
Woodbridge 1.148
Houston 761
Chandler 744
Ashburn 705
Milan 697
Fairfield 680
Jacksonville 590
Santa Clara 522
Sofia 402
Singapore 338
Shanghai 298
Seattle 280
Munich 277
Wilmington 266
Ottawa 259
Beijing 257
New York 255
Hong Kong 242
Cambridge 240
Mcallen 211
Montréal 211
Boardman 176
Bern 175
Nanjing 173
Princeton 171
Lawrence 156
Abidjan 154
Serra 120
Florence 117
Des Moines 115
Jüchen 108
Izmir 103
Dearborn 100
Lagos 98
Medford 92
Dong Ket 64
Istanbul 63
Nanchang 62
Kunming 55
Rome 44
Livorno 41
Redwood City 38
Council Bluffs 37
Dakar 37
Boulder 35
Ogden 32
San Diego 30
Brussels 28
Shenyang 27
Tianjin 26
Chicago 23
Changsha 22
Hefei 22
Hebei 20
Jiaxing 20
London 20
Norwalk 19
Los Angeles 16
Washington 16
Verona 15
Amsterdam 14
Pisa 14
São Paulo 14
Baghdad 13
Guangzhou 13
Pune 13
Cotonou 12
Orange 11
Auburn Hills 10
Hangzhou 10
Massa 10
Dallas 9
Lanzhou 9
Padova 9
Chengdu 8
Dublin 8
Alessandria 7
Fuzhou 7
Helsinki 7
Monsummano Terme 7
Indiana 6
Phoenix 6
Changchun 5
Falkenstein 5
Frankfurt am Main 5
Hanoi 5
Hyderabad 5
Mexico City 5
Osimo 5
Quanzhou 5
Santiago 5
Warangal 5
Belo Horizonte 4
Campinas 4
Chongqing 4
Curitiba 4
Córdoba 4
Drogheda 4
Duncan 4
Totale 13.526
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Nome #
Ecco come ‘Industria 4.0’ migliora l’industria di processo (Il Monitoraggio delle Prestazioni degli Impianti nello Scenario dell’Industria 4.0) 320
A Comparison of Techniques for Automatic Detection of Stiction: Simulation and Application to Industrial Data 317
null 312
Non linear standard regulators 294
An augmented PID control structure to compensate for valve stiction 268
null 237
Improved Qualitative Shape Analysis Technique for Automatic Detection of Valve Stiction in Flow Control loops 218
ROBUST TUNING OF CONVENTIONAL CONTROLLERS 203
Numerical investigation of the mixing of highly viscous liquids with Cowles impellers 199
A New Performance Evaluation Strategy for Decentralized Multivariable PID Control Systems 188
A Two-Phase flow model for Geothermal Wells in the Presence of Non-Condensable Gas 186
A Characterization of Oscillating Phenomena on Sieve Plates of Transfer Columns 177
System identification applied to stiction quantification in industrial control loops: A comparative study 167
Tuning of Conventional Controllers for Robust Performance 165
A METHOD FOR ROBUST TUNING OF LINEAR-QUADRATIC OPTIMAL CONTROLLERS 164
Biomethane Production: Mass and Energy Balances of Alternative Supply Chains 164
Identification techniques for stiction quantification in the presence of nonstationary disturbances 163
PERFORMANCE OF DIFFERENT REGULATORS FOR PLANTS WITH RECYCLE 160
Control of the Quality of Polymer Products in Continuous Reactors: Comparison of Performance of State Estimators with and without Updating of Parameters 160
Variable structure PI controllers in the presence of uncertainty and saturation 159
Enhancing MPC formulations by identification and estimation of valve stiction 158
Analysis of operating conditions of autoaccelerating batch reactors 154
null 147
Issues in on-line Implementation of a Closed Loop Performance System 147
Identification and estimation of valve stiction by the use of a smoothed model 147
Issues in the Control of Systems with Recycle 145
Performance of control systems based on recycle compensators in integrated plants 144
FEEDFORWARD CONTROL IN THE PRESENCE OF UNCERTAINTY 142
DESIGN OF DOUBLE FILTER IMC CONTROLLER FOR ILL-CONDITIONED DISTILLATION-COLUMNS 141
Optimal operation strategies to control the molecular weight distribution of polymer products 141
Design and Control Selections for Cascade Loops in Distillation 141
Control of Overshoot in the Step Response of Chemical Processes 141
An Application of Lyapounov's Methods for Batch Reactors Stability Studies 138
Controllability Analysis by Plant Oriented Techniques: Application to the Tennessee Eastman Benchmark 138
Controller Design for a Multiproduct Distillation Unit in the Presence of Uncertainty 137
Control of Systems with Recycle by means of Compensators 136
Automatic Detection of Stiction in Actuators: A Technique to Reduce the Number of Uncertain Cases. 136
Accuracy of Autotuning Identification Methods and Achievable Closed Loop Performance 135
COMPARISON OF INTERNAL MODEL CONTROL AND LINEAR QUADRATIC OPTIMAL-CONTROL FOR SISO SYSTEMS 134
Modeling the Prediction of the Effect of the Molecular Weight Distribution of Polymer Products 134
A Data-Base Measure for Interactions in Multivariate Systems 134
Robustness Issues in Feedforward Control 132
A comparison of Relay Techniques for Identification and Autotuning of Chemical Processes 132
Process control performance evaluation in the case of variable set-point with experimental applications 131
Implementation, Parameters Calibration and Field Validation of a Closed Loop Performance Monitoring System 130
Performance of Optimal and Standard Controllers for Disturbance Rejection in Industrial Processes 128
Performance of Control Scheme Based on Estimators in the Control of Continuous Polymerization Reactors 128
Adaptive Control of an Experimental Distillation Column by Relay Methods 126
Closed Loop Performance Monitoring: Automatic Diagnosis of Valve Stiction by means of a Technique based on Shape Analysis Formalism 126
Relay with Additional Delay for Identification and Autotuning of Completely Unknown Processes 126
A Revised Technique of Stiction Compensation for Control Valves 126
Use of Modified Relay Techniques for the Design of Model Based Controllers for Chemical Processes 125
Variable Structure Regulators for Industrial Process Control 124
Identification of Chemical Processes for Control Purposes by Relay Techniques 124
Relay Autotuning of Multivariable systems: Application to an Experimental Pilot-Scale Distillation Column 124
Improved Identification and Autotuning of PI Controllers for MIMO Processes by Relay Techniques 123
Temperature Oscillation Calorimetry: Robustness Analysis of Different Algorithms for the Evaluation of the Heat Transfer Coefficient 123
Preface to Special Issue on Process Control 122
null 119
Analysis and Design of Cascade Control Schemes in Distillation 118
Selection and Tuning of Decentralized Systems for Chemical Processes 117
Dynamics and Control of Chemical Plants with Recycle Streams 117
Sequential versus Simultaneous Relay Techniques for Autotuning of Multivariable Processes 117
Multiloop Autotuning Using Relay Feedback: Limits and Extensions 116
Modeling Disturbance Dynamics to Improve Controller Performance in Industrial Loops 115
Analisi di Schemi di Controllo in Cascata per Processi Chimici 114
Analysis of Molecular Weight Distribution in Free Radical Polymerization 114
Analytical Design of PID Controllers for Inverse Response Processes 114
Comportamento Dinamico e Controllo di un Impianto di Prova per Pompe di Calore 112
null 112
A Cloud-Based Monitoring System for Performance Assessment of Industrial Plants 111
Modelling of Polymerization Reactors: the Influence of Diffusion Phenomena on the Choice of Operating Conditions 110
Algoritmi di Controllo per Regolatori di Processo Non Lineari 108
Performance improvements of cascade and feed-forward control schemes for industrial processes 108
Evaluation of Time Varying Parameters in Polymerization Reactors by means of Temperature Oscillation Calorimetry 107
Comparative performance analysis of an electric actuator for control valves 107
Analisi di Schemi di Doppio Controllo di Composizione per Colonne di Distillazione 106
Closed-Loop Identification and Control of Multivariable Chemical Processes: a Case Study 106
Automatic Diagnosis of Valve Stiction by means of a Qualitative Shape Analysis Technique 104
Sequential Identification and Autotuning by Relay Techniques of Decentralised Controllers for Multivariable Chemical Processes 104
Controllo della Emissione di Idrogeno Solforato da Bacini di Trattamento di Acque di Scarico 103
null 103
Analisi di Strategie di Controllo per Colonne Termicamente Integrate 102
Nitrificazione e Bilancio di Ossigeno nelle Acque Correnti 102
A Method for Determining an Optimal Temperature Profile for Molecular Weight Distribution Control 102
Selection of Control Configurations for the Tennessee Eastman Benchmark 102
Design of Decentralized Controllers by a Relay Technique: Extension of Tuning Rules 102
Analysis of Parametric Sensitivity of Optimal Temperature Profiles in Batch Polymerization 102
Identification and Control of Open Loop Unstable Processes by Relay Methods 102
Identification of Unknown Processes for Autotune Purposes by Relay Tests 100
Controlling Ill-Conditioned Plants: SISO Controllers in Distillation 99
OPTIMIZATION OF BATCH POLYMERIZATION REACTORS - MODELING AND EXPERIMENTAL RESULTS FOR SUSPENSION POLYMERIZATION OF METHYLMETHACRYLATE 99
Study of Diffusion Controlled Polymerization through the Analysis of the Molecular Weight Distribution 99
Control of Polymerization Reactors using State Estimators with Different Time Scales 97
An Industry 4.0 demonstrator for cloud-based performance monitoring and assessment of industrial plants 96
Parameter Extimation in Extended Kalman Filters for Quality Control in Polymerization Reactors 94
Analysis of Molecular Weight Distribution in Polymerization Processes 93
null 93
Diagnostica dell’attrito nelle valvole di regolazione 93
Autotuning of PI controllers via Relay with Hysteresys 89
Totale 13.769
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Categoria #
all - tutte 44.202
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 44.202
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2019/2020756 0 0 0 0 0 0 0 0 0 296 327 133
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
2024/20252.704 36 193 71 203 384 340 404 311 409 353 0 0
Totale 18.580