CINECA IRIS Institutional Research Information System

SCALI, CLAUDIO
 Distribuzione geografica
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Continente #
NA - Nord America 11.992
EU - Europa 7.618
AS - Asia 6.174
SA - Sud America 655
AF - Africa 359
Continente sconosciuto - Info sul continente non disponibili 171
OC - Oceania 8
Totale 26.977
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Nazione #
US - Stati Uniti d'America 11.394
CN - Cina 2.125
FI - Finlandia 2.084
IT - Italia 2.012
SG - Singapore 1.791
SE - Svezia 964
HK - Hong Kong 885
BR - Brasile 565
DE - Germania 553
CA - Canada 507
KR - Corea 469
UA - Ucraina 434
BG - Bulgaria 405
VN - Vietnam 361
GB - Regno Unito 328
TR - Turchia 200
FR - Francia 186
CH - Svizzera 185
PL - Polonia 164
RU - Federazione Russa 158
CI - Costa d'Avorio 155
NG - Nigeria 100
IN - India 83
JP - Giappone 61
MX - Messico 51
SN - Senegal 37
BD - Bangladesh 33
BE - Belgio 33
IQ - Iraq 29
NL - Olanda 28
AR - Argentina 24
ES - Italia 23
PK - Pakistan 15
VE - Venezuela 15
MY - Malesia 14
IE - Irlanda 13
BJ - Benin 12
CL - Cile 12
ZA - Sudafrica 12
CO - Colombia 11
EC - Ecuador 11
ID - Indonesia 11
CZ - Repubblica Ceca 10
IR - Iran 10
PH - Filippine 10
TH - Thailandia 10
CR - Costa Rica 8
JM - Giamaica 8
MA - Marocco 8
NP - Nepal 8
TN - Tunisia 7
TW - Taiwan 7
AE - Emirati Arabi Uniti 6
AL - Albania 5
AU - Australia 5
DZ - Algeria 5
GR - Grecia 5
IL - Israele 5
JO - Giordania 5
LT - Lituania 5
PE - Perù 5
UY - Uruguay 5
UZ - Uzbekistan 5
DO - Repubblica Dominicana 4
EG - Egitto 4
KE - Kenya 4
LK - Sri Lanka 4
OM - Oman 4
PY - Paraguay 4
SV - El Salvador 4
AT - Austria 3
AZ - Azerbaigian 3
BB - Barbados 3
BO - Bolivia 3
ET - Etiopia 3
KZ - Kazakistan 3
LY - Libia 3
NZ - Nuova Zelanda 3
PA - Panama 3
RO - Romania 3
RS - Serbia 3
SA - Arabia Saudita 3
TT - Trinidad e Tobago 3
BH - Bahrain 2
DK - Danimarca 2
GT - Guatemala 2
KG - Kirghizistan 2
LU - Lussemburgo 2
NI - Nicaragua 2
NO - Norvegia 2
PS - Palestinian Territory 2
PT - Portogallo 2
AF - Afghanistan, Repubblica islamica di 1
AM - Armenia 1
AO - Angola 1
BA - Bosnia-Erzegovina 1
BY - Bielorussia 1
CD - Congo 1
CV - Capo Verde 1
CW - ???statistics.table.value.countryCode.CW??? 1
Totale 26.788
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Città #
Helsinki 1.896
Ann Arbor 1.178
Woodbridge 1.148
Ashburn 1.031
Singapore 1.029
Hong Kong 875
Houston 769
Chandler 744
Milan 705
Fairfield 680
Hefei 626
Jacksonville 590
Santa Clara 540
San Jose 499
Seoul 464
Sofia 402
Dallas 370
Beijing 319
Shanghai 301
Munich 296
Seattle 282
New York 274
Wilmington 267
Ottawa 259
Cambridge 240
Mcallen 211
Montréal 211
Boardman 177
Bern 175
Nanjing 174
Princeton 171
Lawrence 156
Abidjan 155
Council Bluffs 153
Lauterbourg 140
Serra 120
Des Moines 117
Florence 117
Jüchen 108
Los Angeles 108
Izmir 105
Dearborn 100
Lagos 99
Medford 92
Ho Chi Minh City 80
Buffalo 69
Istanbul 68
Dong Ket 64
Nanchang 62
Tokyo 56
Kunming 55
Rome 54
Hanoi 51
São Paulo 47
Livorno 41
Redondo Beach 40
Redwood City 38
Chicago 37
Dakar 37
Boulder 35
Ogden 32
San Diego 31
Brussels 28
Shenyang 27
Tianjin 27
London 24
Changsha 23
Hebei 20
Jiaxing 20
Orem 20
Columbus 19
Norwalk 19
Pisa 19
Amsterdam 17
Baghdad 17
Hangzhou 16
The Dalles 16
Washington 16
Frankfurt am Main 15
Guangzhou 15
Verona 15
Belo Horizonte 14
Pune 13
Chennai 12
Cotonou 12
Dhaka 12
Phoenix 12
Atlanta 11
Brooklyn 11
Orange 11
Paris 11
Turku 11
Auburn Hills 10
Brasília 10
Campinas 10
Curitiba 10
Massa 10
Da Nang 9
Dublin 9
Fortaleza 9
Totale 19.950
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Nome #
Non linear standard regulators 2.213
Ecco come ‘Industria 4.0’ migliora l’industria di processo (Il Monitoraggio delle Prestazioni degli Impianti nello Scenario dell’Industria 4.0) 375
A Comparison of Techniques for Automatic Detection of Stiction: Simulation and Application to Industrial Data 358
An augmented PID control structure to compensate for valve stiction 318
null 312
A Two-Phase flow model for Geothermal Wells in the Presence of Non-Condensable Gas 268
Numerical investigation of the mixing of highly viscous liquids with Cowles impellers 267
ROBUST TUNING OF CONVENTIONAL CONTROLLERS 265
Improved Qualitative Shape Analysis Technique for Automatic Detection of Valve Stiction in Flow Control loops 241
null 237
A Characterization of Oscillating Phenomena on Sieve Plates of Transfer Columns 232
Analysis of operating conditions of autoaccelerating batch reactors 221
A New Performance Evaluation Strategy for Decentralized Multivariable PID Control Systems 221
Variable structure PI controllers in the presence of uncertainty and saturation 219
A METHOD FOR ROBUST TUNING OF LINEAR-QUADRATIC OPTIMAL CONTROLLERS 217
Biomethane Production: Mass and Energy Balances of Alternative Supply Chains 216
Tuning of Conventional Controllers for Robust Performance 213
Control of the Quality of Polymer Products in Continuous Reactors: Comparison of Performance of State Estimators with and without Updating of Parameters 213
Identification and estimation of valve stiction by the use of a smoothed model 213
Enhancing MPC formulations by identification and estimation of valve stiction 213
System identification applied to stiction quantification in industrial control loops: A comparative study 211
Identification techniques for stiction quantification in the presence of nonstationary disturbances 207
PERFORMANCE OF DIFFERENT REGULATORS FOR PLANTS WITH RECYCLE 202
An Application of Lyapounov's Methods for Batch Reactors Stability Studies 194
COMPARISON OF INTERNAL MODEL CONTROL AND LINEAR QUADRATIC OPTIMAL-CONTROL FOR SISO SYSTEMS 191
FEEDFORWARD CONTROL IN THE PRESENCE OF UNCERTAINTY 190
Controller Design for a Multiproduct Distillation Unit in the Presence of Uncertainty 189
Optimal operation strategies to control the molecular weight distribution of polymer products 188
Control of Systems with Recycle by means of Compensators 187
Design and Control Selections for Cascade Loops in Distillation 185
DESIGN OF DOUBLE FILTER IMC CONTROLLER FOR ILL-CONDITIONED DISTILLATION-COLUMNS 184
Performance of Control Scheme Based on Estimators in the Control of Continuous Polymerization Reactors 184
Issues in the Control of Systems with Recycle 184
Issues in on-line Implementation of a Closed Loop Performance System 184
Process control performance evaluation in the case of variable set-point with experimental applications 183
Robustness Issues in Feedforward Control 176
Algoritmi di Controllo per Regolatori di Processo Non Lineari 175
Variable Structure Regulators for Industrial Process Control 175
Analisi di Schemi di Controllo in Cascata per Processi Chimici 174
Performance of Optimal and Standard Controllers for Disturbance Rejection in Industrial Processes 174
Controllability Analysis by Plant Oriented Techniques: Application to the Tennessee Eastman Benchmark 172
Modeling the Prediction of the Effect of the Molecular Weight Distribution of Polymer Products 170
Improved Identification and Autotuning of PI Controllers for MIMO Processes by Relay Techniques 170
Temperature Oscillation Calorimetry: Robustness Analysis of Different Algorithms for the Evaluation of the Heat Transfer Coefficient 170
Analysis and Design of Cascade Control Schemes in Distillation 168
Preface to Special Issue on Process Control 168
Automatic Detection of Stiction in Actuators: A Technique to Reduce the Number of Uncertain Cases. 168
A Revised Technique of Stiction Compensation for Control Valves 168
Implementation, Parameters Calibration and Field Validation of a Closed Loop Performance Monitoring System 166
Adaptive Control of an Experimental Distillation Column by Relay Methods 165
Control of Overshoot in the Step Response of Chemical Processes 165
Comportamento Dinamico e Controllo di un Impianto di Prova per Pompe di Calore 164
Dynamics and Control of Chemical Plants with Recycle Streams 164
Performance of control systems based on recycle compensators in integrated plants 164
Modelling of Polymerization Reactors: the Influence of Diffusion Phenomena on the Choice of Operating Conditions 162
Selection and Tuning of Decentralized Systems for Chemical Processes 160
A Data-Base Measure for Interactions in Multivariate Systems 160
Comparative performance analysis of an electric actuator for control valves 160
Multiloop Autotuning Using Relay Feedback: Limits and Extensions 159
Analisi di Strategie di Controllo per Colonne Termicamente Integrate 158
A comparison of Relay Techniques for Identification and Autotuning of Chemical Processes 158
Accuracy of Autotuning Identification Methods and Achievable Closed Loop Performance 158
Analisi di Schemi di Doppio Controllo di Composizione per Colonne di Distillazione 157
OPTIMIZATION OF BATCH POLYMERIZATION REACTORS - MODELING AND EXPERIMENTAL RESULTS FOR SUSPENSION POLYMERIZATION OF METHYLMETHACRYLATE 156
Analysis of Molecular Weight Distribution in Free Radical Polymerization 156
Nitrificazione e Bilancio di Ossigeno nelle Acque Correnti 155
Relay Autotuning of Multivariable systems: Application to an Experimental Pilot-Scale Distillation Column 155
Relay with Additional Delay for Identification and Autotuning of Completely Unknown Processes 154
Closed Loop Performance Monitoring: Automatic Diagnosis of Valve Stiction by means of a Technique based on Shape Analysis Formalism 153
Controllo della Emissione di Idrogeno Solforato da Bacini di Trattamento di Acque di Scarico 152
Analytical Design of PID Controllers for Inverse Response Processes 151
Use of Modified Relay Techniques for the Design of Model Based Controllers for Chemical Processes 150
Study of Diffusion Controlled Polymerization through the Analysis of the Molecular Weight Distribution 149
Analysis of Molecular Weight Distribution in Polymerization Processes 148
Identification of Chemical Processes for Control Purposes by Relay Techniques 148
Performance improvements of cascade and feed-forward control schemes for industrial processes 148
A Cloud-Based Monitoring System for Performance Assessment of Industrial Plants 148
null 147
Selection of Control Configurations for the Tennessee Eastman Benchmark 147
Sequential versus Simultaneous Relay Techniques for Autotuning of Multivariable Processes 147
A Method for Determining an Optimal Temperature Profile for Molecular Weight Distribution Control 146
An Industry 4.0 demonstrator for cloud-based performance monitoring and assessment of industrial plants 146
Robustness evaluation of different controllers in the presence of flow rate variations 146
Parameter Extimation in Extended Kalman Filters for Quality Control in Polymerization Reactors 145
Control of Polymerization Reactors using State Estimators with Different Time Scales 144
Analysis of Parametric Sensitivity of Optimal Temperature Profiles in Batch Polymerization 144
Controlling Ill-Conditioned Plants: SISO Controllers in Distillation 143
Modeling Disturbance Dynamics to Improve Controller Performance in Industrial Loops 142
Identification of Unknown Processes for Autotune Purposes by Relay Tests 139
Identification and Control of Open Loop Unstable Processes by Relay Methods 139
Evaluation of Time Varying Parameters in Polymerization Reactors by means of Temperature Oscillation Calorimetry 139
Autotuning of PI controllers via Relay with Hysteresys 137
Automatic Diagnosis of Valve Stiction by means of a Qualitative Shape Analysis Technique 137
Soluzione di Problemi di Interazione nel Controllo di Colonne di Distillazione mediante Disaccoppiamento Implicito 135
Design of Decentralized Controllers by a Relay Technique: Extension of Tuning Rules 134
Il Centro ARPAT per il Controllo delle Emissioni e la Prevenzione dell'Inquinamento Atmosferico nel Comprensorio del Cuoio 133
Sequential Identification and Autotuning by Relay Techniques of Decentralised Controllers for Multivariable Chemical Processes 133
Closed-Loop Identification and Control of Multivariable Chemical Processes: a Case Study 131
Control of Polymerization Reactors by Means of Different State Estimators 129
"Adattamento in Linea di Regolatori PID per Reattori di Polimerizzazione in Condizioni Operative Instabili" 129
Totale 19.878
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Categoria #
all - tutte 65.380
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 65.380
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2021/20221.652 0 125 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
2025/20266.386 304 869 531 314 310 508 720 205 2.037 397 103 88
2026/2027223 116 107 0 0 0 0 0 0 0 0 0 0
Totale 26.977