SCALABRIN, GIANCARLO
 Distribuzione geografica
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Continente #
NA - Nord America 3.941
AS - Asia 1.403
EU - Europa 857
SA - Sud America 357
AF - Africa 298
OC - Oceania 27
Continente sconosciuto - Info sul continente non disponibili 19
Totale 6.902
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Nazione #
US - Stati Uniti d'America 3.758
SG - Singapore 499
VN - Vietnam 260
BR - Brasile 216
HK - Hong Kong 177
CN - Cina 135
UA - Ucraina 131
FI - Finlandia 97
DE - Germania 91
SE - Svezia 88
FR - Francia 51
PL - Polonia 45
GB - Regno Unito 39
RU - Federazione Russa 37
AR - Argentina 28
IT - Italia 28
ID - Indonesia 20
EC - Ecuador 17
IQ - Iraq 17
IR - Iran 17
CO - Colombia 16
ZA - Sudafrica 16
IE - Irlanda 15
KZ - Kazakistan 15
PR - Porto Rico 15
AO - Angola 14
JP - Giappone 14
ML - Mali 14
MN - Mongolia 14
PY - Paraguay 14
BE - Belgio 13
EG - Egitto 13
ES - Italia 13
NL - Olanda 13
UZ - Uzbekistan 13
VE - Venezuela 13
CA - Canada 12
CZ - Repubblica Ceca 12
HN - Honduras 12
IN - India 12
MX - Messico 12
NI - Nicaragua 12
PE - Perù 12
TH - Thailandia 12
TT - Trinidad e Tobago 12
AZ - Azerbaigian 11
BO - Bolivia 11
BZ - Belize 11
CL - Cile 11
CW - ???statistics.table.value.countryCode.CW??? 11
DZ - Algeria 11
ET - Etiopia 11
GE - Georgia 11
HU - Ungheria 11
JM - Giamaica 11
JO - Giordania 11
MD - Moldavia 11
MG - Madagascar 11
MW - Malawi 11
PH - Filippine 11
RW - Ruanda 11
TN - Tunisia 11
GF - Guiana Francese 10
KH - Cambogia 10
MY - Malesia 10
PT - Portogallo 10
RE - Reunion 10
SK - Slovacchia (Repubblica Slovacca) 10
TW - Taiwan 10
UG - Uganda 10
AE - Emirati Arabi Uniti 9
AL - Albania 9
BA - Bosnia-Erzegovina 9
CU - Cuba 9
EE - Estonia 9
GH - Ghana 9
KG - Kirghizistan 9
KR - Corea 9
NO - Norvegia 9
NP - Nepal 9
PA - Panama 9
SA - Arabia Saudita 9
SI - Slovenia 9
UY - Uruguay 9
YE - Yemen 9
BY - Bielorussia 8
CD - Congo 8
GM - Gambi 8
KE - Kenya 8
LC - Santa Lucia 8
ME - Montenegro 8
NA - Namibia 8
NZ - Nuova Zelanda 8
SN - Senegal 8
VC - Saint Vincent e Grenadine 8
AD - Andorra 7
BF - Burkina Faso 7
CI - Costa d'Avorio 7
CV - Capo Verde 7
DM - Dominica 7
Totale 6.601
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Città #
Jacksonville 536
Fairfield 468
Woodbridge 302
Singapore 284
Santa Clara 281
Ashburn 248
Houston 239
Wilmington 203
Seattle 195
Cambridge 182
Chandler 181
Dong Ket 181
Hong Kong 172
Princeton 160
Ann Arbor 159
Boardman 85
San Diego 54
Ho Chi Minh City 38
Nanjing 36
Helsinki 32
Bytom 30
Roxbury 19
Los Angeles 18
São Paulo 17
Hanoi 16
Ulan Bator 14
Luanda 13
New York 13
Tashkent 13
Bamako 12
Managua 12
Norwalk 12
Baku 11
Hebei 11
Willemstad 11
Amman 10
Buffalo 10
Kampala 10
Lilongwe 10
Phnom Penh 10
Rio de Janeiro 10
Shenyang 10
Accra 9
Dublin 9
Kigali 9
Nanchang 9
Panama City 9
Quito 9
Addis Ababa 8
Bishkek 8
Castries 8
Cayenne 8
Dakar 8
Des Moines 8
Falkenstein 8
Havana 8
Kingstown 8
Montevideo 8
Tallinn 8
Tokyo 8
Andorra la Vella 7
Antananarivo 7
Auckland 7
Bangkok 7
Belo Horizonte 7
Brussels 7
Guayaquil 7
Kinshasa 7
Lima 7
Minsk 7
Podgorica 7
Roseau 7
San Pedro Sula 7
Sanaa 7
Tbilisi 7
Warsaw 7
Abidjan 6
Asunción 6
Belize City 6
Brazzaville 6
Cairo 6
Chisinau 6
Conakry 6
Dili 6
Dushanbe 6
Guangzhou 6
London 6
Nairobi 6
Prague 6
Praia 6
Riga 6
Salt Lake City 6
San José 6
San Juan 6
Tunis 6
Vienna 6
Baghdad 5
Banjul 5
Bogotá 5
Brooklyn 5
Totale 4.730
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Nome #
Bubble pressure measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system. 190
A viscosity equation of state for R134a through a multi-layer feedforward neural network technique. 170
A multiparameter viscosity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 164
A method for the prediction of vapour-liquid equilibria of refrigerant mixtures at low and moderate pressure 162
A reference multiparameter thermal conductivity equation for carbon dioxide with an optimized functional form. 161
An equation of state for R227ea from density data through a new extended corresponding states - neural network technique 160
A multiparameter thermal conductivity equation for R134a with an optimized functional form. 154
A reference multiparameter viscosity equation for R134a in optimized functional form. 151
A fundamental equation of state for the (R134a + triethylene glycol dimethyl ether) mixture. 151
Enhancement of the extended corresponding states techniques for thermodynamic modeling. II. Mixtures. 146
An extended equation of state modeling method. I. Pure fluids. 144
Compressed and saturated liquid densities for 2–propanol + water system. 143
A reference multiparameter viscosity equation for propane with an optimized functional form. 142
Analysis of forced convection heat transfer to supercritical carbon dioxide inside tubes using neural networks. 142
Flow boiling of pure fluids: local heat transfer and flow pattern modeling through artificial neural networks. 139
A Corresponding States Helmholtz free energy model based on a conformality analysis 136
An extended equation of state modeling method. II. Mixtures. 136
A multiparameter thermal conductivity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 133
A fundamental equation of state for sulfur hexafluoride (SF6) in the extended equation of state format. 131
A fundamental equation of state for 2-propanol (C3H8O) in the extended equation of state format. 131
Enhancement of the extended corresponding states techniques for thermodynamic modeling. I. Pure fluids. 131
A predictive density model in a corresponding states format. Application to pure and mixed refrigerants 130
A corresponding states predictive model for saturated liquid density of halogenated alkanes and fluorinated propanes and ethers 130
Mixtures flow boiling: modeling heat transfer through artificial neural networks. 127
Development of a fundamental equation of state for the liquid region of a pure fluid from speed of sound measurements. Application to water. 127
Liquid density and bubble pressure measurements for propylene + 2-propanol system. 125
Speed of sound predictive modeling in a three-parameter corresponding states format. Application to pure and mixed haloalkanes. 122
Density measurements of liquid 2-propanol at temperatures between (280 and 393) K and at pressures up to 10 MPa. 119
A corresponding states thermodynamic model for pure and mixed refrigerants in terms of the Helmholtz energy 118
A fundamental equation of state for the mixture ammonia-water in an innovative extended equation of state format. 116
A new three-parameter corresponding states model for pure halocarbons viscosity prediction. 116
Heuristic modeling for thermodynamics: state of the art and prospects. Invited lecture. 113
A viscosity equation of state for R123 in the form of a multilayer feed forward 112
Modeling flow boiling heat transfer of pure fluids through artificial neural networks. 111
Vapor phase acoustic measurements for R125 and development of an Helmholtz free energy equation 111
Forced convective heat transfer to supercritical carbon dioxide inside tubes. Analysis through neural networks. 108
A corresponding states predictive viscosity model based on a new scaling parameter: Application to hydrocarbons, halocarbons and mixtures. 104
Vapor-liquid-liquid equilibria and excess molar enthalpies of binary and ternary mixtures of 2-propanol, water and propylene. 103
The viscosity surfaces of R152a in the form of multilayer feed forward neural networks. 99
Modelling enthalpy and entropy of pure and mixed refrigerants with an innovative corresponding states method. 98
P,Rho,T,x measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethylether) at high haloalkane content. 98
Liquid density measurements for the propylene + 2-propanol + water system. 98
A direct reduction procedure for gas densities determination of R143a from acoustic measurements 97
The viscosity correlation for ethane in the form of multilayer feedforward neural networks 87
Prediction of Vapor-Liquid Equilibria of Refrigerant Mixtures by a Cubic Group-Contribution Equation of State 85
Thermal conductivity modeling of refrigerant mixtures in a three-parameter corresponding states format. 84
Viscosity prediction of pure fluids and mixtures in a corresponding states framework 84
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. I. Modelling techniques. 82
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics. 80
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 76
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. II. Application to two fluids. 74
Convective cooling of supercritical carbon dioxide inside tubes: heat transfer analysis through neural networks. 73
Vapor phase Helmholtz equation for HFC-227ea from speed of sound measurements 71
Prediction of halocarbons mixtures thermodynamics through an innovative gE-EoS mixing rule in a three parameters CS framework 70
Isothermal VLE measurements for the binary mixtures HFC-125+HFC-245fa and HC-290+HFC-245fa, 70
Modelling alkane and haloalkane mixture viscosities in a three-parameter corresponding states format. 69
The viscosity surfaces of propane in the form of multilayer feed forward neural networks. 66
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics 64
Viscosity equations of pure fluids in an innovative extended corresponding states framework. II. Application to four fluids 63
Determination of a vapor phase Helmholtz equation for 1,1,1-trifluoroethane (HFC-143a) from speed-of-sound measurements 58
Compressed liquid and supercritical densities of 1,1,1,2,3,3,3-heptafluoropropane (R227ea). 55
Totale 6.910
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Categoria #
all - tutte 18.217
article - articoli 16.962
book - libri 0
conference - conferenze 0
curatela - curatele 0
other - altro 0
patent - brevetti 0
selected - selezionate 0
volume - volumi 0
Totale 35.179
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2020/2021585 0 0 0 0 0 54 12 72 120 41 81 205
2021/2022569 13 60 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
2025/20261.782 83 286 581 575 251 6 0 0 0 0 0 0
Totale 6.910