Viscosity GasoilProgram calcul vascozitate titeifunctie de temperaturaLog(niu)=B*(559.67/(T+459.67))S-0.86960whereniu =kinematic viscozity at temperature T, in centistokesT=temperature ,in degrees Fahreinheitniu 0=measured kinematic viscosity at 100 F, in centistokesB =Log( niu 0)+0.86960S=0.28008*Log( niu 0)+1.8616Exemplu de calcul vascozitate titei Sumatran crudeniu 01.38cSt205cStB1.00953.1814S1.90082.5091T210.0degrees ,F210.0degrees ,Flog( niu)-0.15191.1585niu0.705cSt14.404cSttitei Sumatrantitei soroosh pentru verificare formulamotorina Petrobrazi t=-4 0Cniu 02cStB1.1706S1.9459t-20.00000CT-4.00Flog( niu)0.8768niu7.531cStmotorina Petrobrazi t=100 0Cniu 02cStB1.1706S1.9459t100.000CT212.00Flog( niu)-0.0488niu0.894cStKEROSENE Petrobrazi t=15Cniu 01.6cStB1.0737S1.9188t15.00000CT59.00Flog( niu)0.3729niu2.360cStKEROSENE Petrobrazi t=20 0Cniu 01.6cStB1.0737S1.9188t-20.000CT-4.00Flog( niu)0.7233niu5.289cSt

FAMEProgram calcul vascozitate titeifunctie de temperaturaLog(niu)=B*(559.67/(T+459.67))S-0.86960whereniu =kinematic viscozity at temperature T, in centistokesT=temperature ,in degrees Fahreinheitniu 0=measured kinematic viscosity at 100 F, in centistokesB =Log( niu 0)+0.86960S=0.28008*Log( niu 0)+1.8616Exemplu de calcul vascozitate titei Sumatran crudeniu 01.38cSt205cStB1.00953.1814S1.90082.5091T210.0degrees ,F210.0degrees ,Flog( niu)-0.15191.1585niu0.705cSt14.404cSttitei Sumatrantitei soroosh pentru verificare formulaFAME Petrobrazi t=+ 15 0Cniu 04.4cStB1.5131S2.0418t15.00000CT59.00Flog( niu)0.8977niu7.902cStFAME Petrobrazi t=50 0Cniu 04.4cStB1.5131S2.0418t100.000CT212.00Flog( niu)0.1729niu1.489cStFAME Petrobrazi t=25Cniu 04.4cStB1.5131S2.0418t25.00000CT77.00Flog( niu)0.7788niu6.009cStFAME Petrobrazi t=35 0CFAME Petrobrazi t=15 0Cniu 04.4cStniu 04.4cStB1.5131B1.5131S2.0418S2.0418t35.000Ct15.000CT95.00FT59.00Flog( niu)0.6714log( niu)0.8977niu4.693cStniu7.902cStBENZINA ROSNEFTniu 00.9cStB0.8238S1.8488t-50.000CT-58.00Flog( niu)0.6516niu4.483cSt

Foaie3

PROPANEProgram calcul vascozitate titeifunctie de temperaturaLog(niu)=B*(559.67/(T+459.67))S-0.86960whereniu =kinematic viscozity at temperature T, in centistokesT=temperature ,in degrees Fahreinheitniu 0=measured kinematic viscosity at 100 F, in centistokesB =Log( niu 0)+0.86960S=0.28008*Log( niu 0)+1.8616Exemplu de calcul vascozitate titei Sumatran crudeniu 01.38cSt205cStB1.00953.1814S1.90082.5091T210.0degrees ,F210.0degrees ,Flog( niu)-0.15191.1585niu0.705cSt14.404cSttitei Sumatrantitei soroosh pentru verificare formulaPropan Lichid t=+ 30 0Cniu 00.2cSt@t=37.8 0CB0.1706S1.6658t30.00000CT86.00Flog( niu)-0.6916niu0.203cStn-butan t=30 0Cniu 00.264cStB0.2912S1.6996t30.000CT86.00Flog( niu)-0.5656niu0.272cStFAME Petrobrazi t=25Cniu 04.4cStB1.5131S2.0418t25.00000CT77.00Flog( niu)0.7788niu6.009cStFAME Petrobrazi t=35 0Cniu 04.4cStB1.5131S2.0418t35.000CT95.00Flog( niu)0.6714niu4.693cStBENZINA ROSNEFTniu 00.9cStB0.8238S1.8488t-50.000CT-58.00Flog( niu)0.6516niu4.483cSt

cSt@t=37.8 0C