SCALABRIN, GIANCARLO
 Distribuzione geografica
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Continente #
NA - Nord America 5.022
AS - Asia 2.183
EU - Europa 982
SA - Sud America 424
AF - Africa 340
Continente sconosciuto - Info sul continente non disponibili 29
OC - Oceania 28
Totale 9.008
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Nazione #
US - Stati Uniti d'America 4.808
SG - Singapore 692
VN - Vietnam 417
CN - Cina 289
BR - Brasile 242
HK - Hong Kong 208
UA - Ucraina 132
FI - Finlandia 103
DE - Germania 102
FR - Francia 102
SE - Svezia 89
IT - Italia 63
IN - India 58
IQ - Iraq 50
PL - Polonia 46
BD - Bangladesh 43
GB - Regno Unito 43
RU - Federazione Russa 40
AR - Argentina 38
ID - Indonesia 29
PH - Filippine 29
PK - Pakistan 27
CO - Colombia 25
JP - Giappone 23
SA - Arabia Saudita 23
EC - Ecuador 22
UZ - Uzbekistan 20
TR - Turchia 19
ZA - Sudafrica 19
CA - Canada 18
IR - Iran 17
KZ - Kazakistan 17
TH - Thailandia 17
AO - Angola 16
EG - Egitto 16
JM - Giamaica 16
JO - Giordania 16
PR - Porto Rico 16
VE - Venezuela 16
CL - Cile 15
HN - Honduras 15
IE - Irlanda 15
MN - Mongolia 15
MX - Messico 15
NL - Olanda 15
PY - Paraguay 15
TN - Tunisia 15
BE - Belgio 14
BO - Bolivia 14
ET - Etiopia 14
ML - Mali 14
MY - Malesia 14
NP - Nepal 14
PE - Perù 14
ES - Italia 13
GE - Georgia 13
AL - Albania 12
AZ - Azerbaigian 12
CW - ???statistics.table.value.countryCode.CW??? 12
CZ - Repubblica Ceca 12
KR - Corea 12
MA - Marocco 12
MD - Moldavia 12
NI - Nicaragua 12
RW - Ruanda 12
TT - Trinidad e Tobago 12
AE - Emirati Arabi Uniti 11
BZ - Belize 11
DZ - Algeria 11
GF - Guiana Francese 11
HU - Ungheria 11
MG - Madagascar 11
MW - Malawi 11
PA - Panama 11
RE - Reunion 11
TW - Taiwan 11
UY - Uruguay 11
KE - Kenya 10
KG - Kirghizistan 10
KH - Cambogia 10
NO - Norvegia 10
PT - Portogallo 10
SK - Slovacchia (Repubblica Slovacca) 10
UG - Uganda 10
BA - Bosnia-Erzegovina 9
CU - Cuba 9
EE - Estonia 9
GH - Ghana 9
NA - Namibia 9
NZ - Nuova Zelanda 9
SI - Slovenia 9
YE - Yemen 9
BF - Burkina Faso 8
BY - Bielorussia 8
CD - Congo 8
CI - Costa d'Avorio 8
CR - Costa Rica 8
GM - Gambi 8
GT - Guatemala 8
LC - Santa Lucia 8
Totale 8.657
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Città #
San Jose 549
Jacksonville 537
Fairfield 468
Singapore 417
Santa Clara 339
Ashburn 319
Woodbridge 302
Houston 244
Wilmington 204
Seattle 200
Hong Kong 192
Cambridge 182
Chandler 181
Dong Ket 181
Princeton 160
Ann Arbor 159
Council Bluffs 97
Boardman 89
Ho Chi Minh City 82
Los Angeles 67
San Diego 54
Lauterbourg 48
Hanoi 42
Helsinki 38
Nanjing 36
Bytom 30
New York 25
Baghdad 24
São Paulo 21
Roxbury 19
Tashkent 19
Amman 15
Da Nang 15
Ulan Bator 15
Chicago 14
Luanda 14
Baku 12
Bamako 12
Managua 12
Norwalk 12
Willemstad 12
Addis Ababa 11
Guangzhou 11
Hebei 11
Panama City 11
Rio de Janeiro 11
Riyadh 11
Shenyang 11
Tokyo 11
Atlanta 10
Beijing 10
Buffalo 10
Kampala 10
Kigali 10
Lahore 10
Lilongwe 10
Orem 10
Phnom Penh 10
San Pedro Sula 10
Accra 9
Bangkok 9
Bishkek 9
Dallas 9
Dublin 9
Guayaquil 9
Lima 9
Montevideo 9
Nanchang 9
Quito 9
Tbilisi 9
Auckland 8
Brooklyn 8
Brussels 8
Castries 8
Cayenne 8
Dakar 8
Des Moines 8
Falkenstein 8
Haiphong 8
Havana 8
Kingston 8
Kingstown 8
Tallinn 8
Tianjin 8
Tunis 8
Warsaw 8
Abidjan 7
Andorra la Vella 7
Antananarivo 7
Asunción 7
Belo Horizonte 7
Cairo 7
Chisinau 7
Dhaka 7
Kinshasa 7
London 7
Medellín 7
Minsk 7
Nairobi 7
Podgorica 7
Totale 5.971
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Nome #
Bubble pressure measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system. 226
A reference multiparameter viscosity equation for R134a in optimized functional form. 226
A multiparameter viscosity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 221
A reference multiparameter thermal conductivity equation for carbon dioxide with an optimized functional form. 217
Compressed and saturated liquid densities for 2–propanol + water system. 203
A viscosity equation of state for R134a through a multi-layer feedforward neural network technique. 198
An extended equation of state modeling method. I. Pure fluids. 198
A method for the prediction of vapour-liquid equilibria of refrigerant mixtures at low and moderate pressure 196
A multiparameter thermal conductivity equation for R134a with an optimized functional form. 188
An equation of state for R227ea from density data through a new extended corresponding states - neural network technique 188
Enhancement of the extended corresponding states techniques for thermodynamic modeling. II. Mixtures. 188
A reference multiparameter viscosity equation for propane with an optimized functional form. 186
A fundamental equation of state for the (R134a + triethylene glycol dimethyl ether) mixture. 185
An extended equation of state modeling method. II. Mixtures. 179
A fundamental equation of state for sulfur hexafluoride (SF6) in the extended equation of state format. 172
A fundamental equation of state for 2-propanol (C3H8O) in the extended equation of state format. 171
A Corresponding States Helmholtz free energy model based on a conformality analysis 170
Liquid density and bubble pressure measurements for propylene + 2-propanol system. 170
Enhancement of the extended corresponding states techniques for thermodynamic modeling. I. Pure fluids. 169
Analysis of forced convection heat transfer to supercritical carbon dioxide inside tubes using neural networks. 167
A multiparameter thermal conductivity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 167
Flow boiling of pure fluids: local heat transfer and flow pattern modeling through artificial neural networks. 165
Speed of sound predictive modeling in a three-parameter corresponding states format. Application to pure and mixed haloalkanes. 164
Development of a fundamental equation of state for the liquid region of a pure fluid from speed of sound measurements. Application to water. 163
A corresponding states predictive model for saturated liquid density of halogenated alkanes and fluorinated propanes and ethers 161
Mixtures flow boiling: modeling heat transfer through artificial neural networks. 159
Heuristic modeling for thermodynamics: state of the art and prospects. Invited lecture. 158
A fundamental equation of state for the mixture ammonia-water in an innovative extended equation of state format. 158
A predictive density model in a corresponding states format. Application to pure and mixed refrigerants 158
Density measurements of liquid 2-propanol at temperatures between (280 and 393) K and at pressures up to 10 MPa. 158
A viscosity equation of state for R123 in the form of a multilayer feed forward 147
A new three-parameter corresponding states model for pure halocarbons viscosity prediction. 144
A corresponding states thermodynamic model for pure and mixed refrigerants in terms of the Helmholtz energy 144
Vapor-liquid-liquid equilibria and excess molar enthalpies of binary and ternary mixtures of 2-propanol, water and propylene. 143
Vapor phase acoustic measurements for R125 and development of an Helmholtz free energy equation 142
Forced convective heat transfer to supercritical carbon dioxide inside tubes. Analysis through neural networks. 137
Liquid density measurements for the propylene + 2-propanol + water system. 135
P,Rho,T,x measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethylether) at high haloalkane content. 134
A corresponding states predictive viscosity model based on a new scaling parameter: Application to hydrocarbons, halocarbons and mixtures. 134
Modeling flow boiling heat transfer of pure fluids through artificial neural networks. 133
The viscosity surfaces of R152a in the form of multilayer feed forward neural networks. 131
Modelling enthalpy and entropy of pure and mixed refrigerants with an innovative corresponding states method. 126
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. I. Modelling techniques. 123
Prediction of Vapor-Liquid Equilibria of Refrigerant Mixtures by a Cubic Group-Contribution Equation of State 120
A direct reduction procedure for gas densities determination of R143a from acoustic measurements 119
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics. 112
The viscosity correlation for ethane in the form of multilayer feedforward neural networks 112
Thermal conductivity modeling of refrigerant mixtures in a three-parameter corresponding states format. 107
The (P,rho,T) behaviour of 1,1,1,2,3,3,3-heptafluoropropane (HFC-227ea) at temperatures between 253 K and 403 K and pressures up to 20 MPa 104
Viscosity prediction of pure fluids and mixtures in a corresponding states framework 104
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. II. Application to two fluids. 101
Vapor phase Helmholtz equation for HFC-227ea from speed of sound measurements 100
Isothermal VLE measurements for the binary mixtures HFC-125+HFC-245fa and HC-290+HFC-245fa, 100
Viscosity equations of pure fluids in an innovative extended corresponding states framework. II. Application to four fluids 96
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics 96
The viscosity surfaces of propane in the form of multilayer feed forward neural networks. 95
Prediction of halocarbons mixtures thermodynamics through an innovative gE-EoS mixing rule in a three parameters CS framework 93
Convective cooling of supercritical carbon dioxide inside tubes: heat transfer analysis through neural networks. 93
Modelling alkane and haloalkane mixture viscosities in a three-parameter corresponding states format. 92
Compressed liquid and supercritical densities of 1,1,1,2,3,3,3-heptafluoropropane (R227ea). 84
Determination of a vapor phase Helmholtz equation for 1,1,1-trifluoroethane (HFC-143a) from speed-of-sound measurements 78
Totale 9.008
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Categoria #
all - tutte 23.361
article - articoli 21.676
book - libri 0
conference - conferenze 0
curatela - curatele 0
other - altro 0
patent - brevetti 0
selected - selezionate 0
volume - volumi 0
Totale 45.037
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2021/2022496 0 0 71 72 41 18 9 57 49 6 78 95
2022/2023446 135 22 8 36 81 65 0 27 51 2 16 3
2023/2024145 7 32 17 11 5 9 1 2 2 0 18 41
2024/20251.163 0 118 42 49 326 16 21 80 86 32 187 206
2025/20263.487 83 286 581 575 251 150 273 398 477 230 113 70
2026/2027393 171 158 64 0 0 0 0 0 0 0 0 0
Totale 9.008