SCALABRIN, GIANCARLO
 Distribuzione geografica
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Continente #
NA - Nord America 3.891
AS - Asia 1.196
EU - Europa 832
SA - Sud America 289
AF - Africa 272
OC - Oceania 24
Continente sconosciuto - Info sul continente non disponibili 17
Totale 6.521
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Nazione #
US - Stati Uniti d'America 3.720
SG - Singapore 375
VN - Vietnam 216
HK - Hong Kong 175
BR - Brasile 171
UA - Ucraina 130
CN - Cina 126
FI - Finlandia 95
DE - Germania 90
SE - Svezia 88
FR - Francia 51
PL - Polonia 43
GB - Regno Unito 38
RU - Federazione Russa 37
IT - Italia 28
AR - Argentina 21
ID - Indonesia 17
IE - Irlanda 15
IQ - Iraq 15
IR - Iran 15
KZ - Kazakistan 15
PR - Porto Rico 15
EC - Ecuador 14
ML - Mali 14
AO - Angola 13
CO - Colombia 13
EG - Egitto 13
MN - Mongolia 13
PY - Paraguay 13
ZA - Sudafrica 13
ES - Italia 12
NI - Nicaragua 12
NL - Olanda 12
TT - Trinidad e Tobago 12
UZ - Uzbekistan 12
BE - Belgio 11
BZ - Belize 11
CZ - Repubblica Ceca 11
ET - Etiopia 11
HU - Ungheria 11
JP - Giappone 11
MD - Moldavia 11
PE - Perù 11
RW - Ruanda 11
TH - Thailandia 11
TN - Tunisia 11
VE - Venezuela 11
BO - Bolivia 10
CA - Canada 10
CL - Cile 10
CW - ???statistics.table.value.countryCode.CW??? 10
GE - Georgia 10
IN - India 10
JO - Giordania 10
KH - Cambogia 10
MW - Malawi 10
MX - Messico 10
PH - Filippine 10
PT - Portogallo 10
TW - Taiwan 10
AE - Emirati Arabi Uniti 9
AL - Albania 9
AZ - Azerbaigian 9
CU - Cuba 9
GF - Guiana Francese 9
GH - Ghana 9
HN - Honduras 9
JM - Giamaica 9
KG - Kirghizistan 9
KR - Corea 9
MG - Madagascar 9
NP - Nepal 9
PA - Panama 9
RE - Reunion 9
SA - Arabia Saudita 9
UG - Uganda 9
YE - Yemen 9
CD - Congo 8
DZ - Algeria 8
EE - Estonia 8
GM - Gambi 8
LC - Santa Lucia 8
ME - Montenegro 8
MY - Malesia 8
NO - Norvegia 8
SI - Slovenia 8
SK - Slovacchia (Repubblica Slovacca) 8
SN - Senegal 8
AD - Andorra 7
BA - Bosnia-Erzegovina 7
BY - Bielorussia 7
CV - Capo Verde 7
DM - Dominica 7
HT - Haiti 7
IS - Islanda 7
LA - Repubblica Popolare Democratica del Laos 7
LU - Lussemburgo 7
LV - Lettonia 7
NA - Namibia 7
NG - Nigeria 7
Totale 6.249
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Città #
Jacksonville 536
Fairfield 468
Woodbridge 302
Santa Clara 281
Singapore 259
Houston 239
Ashburn 233
Wilmington 203
Seattle 195
Cambridge 182
Chandler 181
Dong Ket 181
Hong Kong 170
Princeton 160
Ann Arbor 159
Boardman 85
San Diego 54
Nanjing 36
Bytom 30
Helsinki 30
Ho Chi Minh City 19
Roxbury 19
Los Angeles 16
New York 13
Ulan Bator 13
Bamako 12
Luanda 12
Managua 12
Norwalk 12
Tashkent 12
Hebei 11
São Paulo 11
Buffalo 10
Phnom Penh 10
Shenyang 10
Willemstad 10
Accra 9
Amman 9
Baku 9
Dublin 9
Hanoi 9
Kampala 9
Kigali 9
Lilongwe 9
Nanchang 9
Panama City 9
Addis Ababa 8
Bishkek 8
Castries 8
Dakar 8
Des Moines 8
Falkenstein 8
Havana 8
Andorra la Vella 7
Cayenne 7
Kingstown 7
Kinshasa 7
Lima 7
Podgorica 7
Quito 7
Roseau 7
Sanaa 7
Tallinn 7
Tbilisi 7
Antananarivo 6
Asunción 6
Bangkok 6
Belize City 6
Belo Horizonte 6
Brussels 6
Cairo 6
Chisinau 6
Dili 6
Dushanbe 6
Guangzhou 6
Guayaquil 6
London 6
Minsk 6
Praia 6
Riga 6
San José 6
San Juan 6
Tokyo 6
Tunis 6
Vienna 6
Abidjan 5
Auckland 5
Banjul 5
Bogotá 5
Brazzaville 5
Brooklyn 5
Chicago 5
Conakry 5
Council Bluffs 5
Medford 5
Montevideo 5
Nairobi 5
Noumea 5
Porto 5
Prague 5
Totale 4.610
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Nome #
Bubble pressure measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethyl ether) system. 183
A viscosity equation of state for R134a through a multi-layer feedforward neural network technique. 166
A method for the prediction of vapour-liquid equilibria of refrigerant mixtures at low and moderate pressure 158
A multiparameter viscosity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 154
A reference multiparameter thermal conductivity equation for carbon dioxide with an optimized functional form. 153
An equation of state for R227ea from density data through a new extended corresponding states - neural network technique 152
A multiparameter thermal conductivity equation for R134a with an optimized functional form. 145
Enhancement of the extended corresponding states techniques for thermodynamic modeling. II. Mixtures. 141
A fundamental equation of state for the (R134a + triethylene glycol dimethyl ether) mixture. 141
Analysis of forced convection heat transfer to supercritical carbon dioxide inside tubes using neural networks. 137
A reference multiparameter viscosity equation for R134a in optimized functional form. 136
A reference multiparameter viscosity equation for propane with an optimized functional form. 135
Flow boiling of pure fluids: local heat transfer and flow pattern modeling through artificial neural networks. 133
A Corresponding States Helmholtz free energy model based on a conformality analysis 133
An extended equation of state modeling method. I. Pure fluids. 133
Compressed and saturated liquid densities for 2–propanol + water system. 132
Enhancement of the extended corresponding states techniques for thermodynamic modeling. I. Pure fluids. 127
A multiparameter thermal conductivity equation for 1,1-difluoroethane (R152a) with an optimized functional form. 125
An extended equation of state modeling method. II. Mixtures. 125
Mixtures flow boiling: modeling heat transfer through artificial neural networks. 124
A corresponding states predictive model for saturated liquid density of halogenated alkanes and fluorinated propanes and ethers 123
A fundamental equation of state for sulfur hexafluoride (SF6) in the extended equation of state format. 121
A fundamental equation of state for 2-propanol (C3H8O) in the extended equation of state format. 120
Development of a fundamental equation of state for the liquid region of a pure fluid from speed of sound measurements. Application to water. 118
A predictive density model in a corresponding states format. Application to pure and mixed refrigerants 117
Liquid density and bubble pressure measurements for propylene + 2-propanol system. 116
A corresponding states thermodynamic model for pure and mixed refrigerants in terms of the Helmholtz energy 116
Speed of sound predictive modeling in a three-parameter corresponding states format. Application to pure and mixed haloalkanes. 113
A new three-parameter corresponding states model for pure halocarbons viscosity prediction. 112
Density measurements of liquid 2-propanol at temperatures between (280 and 393) K and at pressures up to 10 MPa. 111
Modeling flow boiling heat transfer of pure fluids through artificial neural networks. 108
Heuristic modeling for thermodynamics: state of the art and prospects. Invited lecture. 107
Vapor phase acoustic measurements for R125 and development of an Helmholtz free energy equation 107
Forced convective heat transfer to supercritical carbon dioxide inside tubes. Analysis through neural networks. 106
A fundamental equation of state for the mixture ammonia-water in an innovative extended equation of state format. 106
A viscosity equation of state for R123 in the form of a multilayer feed forward 106
A corresponding states predictive viscosity model based on a new scaling parameter: Application to hydrocarbons, halocarbons and mixtures. 100
The viscosity surfaces of R152a in the form of multilayer feed forward neural networks. 95
Modelling enthalpy and entropy of pure and mixed refrigerants with an innovative corresponding states method. 95
A direct reduction procedure for gas densities determination of R143a from acoustic measurements 95
P,Rho,T,x measurements for (1,1,1,2-tetrafluoroethane + triethylene glycol dimethylether) at high haloalkane content. 94
Vapor-liquid-liquid equilibria and excess molar enthalpies of binary and ternary mixtures of 2-propanol, water and propylene. 93
Liquid density measurements for the propylene + 2-propanol + water system. 88
Thermal conductivity modeling of refrigerant mixtures in a three-parameter corresponding states format. 82
Viscosity prediction of pure fluids and mixtures in a corresponding states framework 82
The viscosity correlation for ethane in the form of multilayer feedforward neural networks 81
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics. 79
Prediction of Vapor-Liquid Equilibria of Refrigerant Mixtures by a Cubic Group-Contribution Equation of State 79
Convective cooling of supercritical carbon dioxide inside tubes: heat transfer analysis through neural networks. 72
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 71
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. I. Modelling techniques. 71
Prediction of halocarbons mixtures thermodynamics through an innovative gE-EoS mixing rule in a three parameters CS framework 68
Vapor phase Helmholtz equation for HFC-227ea from speed of sound measurements 67
Modelling alkane and haloalkane mixture viscosities in a three-parameter corresponding states format. 67
Isothermal VLE measurements for the binary mixtures HFC-125+HFC-245fa and HC-290+HFC-245fa, 66
Thermal conductivity equations of pure fluids in an heuristic extended corresponding states framework. II. Application to two fluids. 63
The viscosity surfaces of propane in the form of multilayer feed forward neural networks. 61
Application of neural networks to a predictive extended corresponding states model for pure halocarbons thermodynamics 60
Determination of a vapor phase Helmholtz equation for 1,1,1-trifluoroethane (HFC-143a) from speed-of-sound measurements 57
Viscosity equations of pure fluids in an innovative extended corresponding states framework. II. Application to four fluids 54
Compressed liquid and supercritical densities of 1,1,1,2,3,3,3-heptafluoropropane (R227ea). 49
Totale 6.529
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Categoria #
all - tutte 17.464
article - articoli 16.270
book - libri 0
conference - conferenze 0
curatela - curatele 0
other - altro 0
patent - brevetti 0
selected - selezionate 0
volume - volumi 0
Totale 33.734
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Totale Lug Ago Sett Ott Nov Dic Gen Feb Mar Apr Mag Giu
2020/2021683 0 0 0 74 24 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
2025/20261.401 83 286 581 451 0 0 0 0 0 0 0 0
Totale 6.529