2 research outputs found
Cracking of Heavy Oil at Presence of Zeolite Y Modified of Nickel Nanopowder
ΠΠ·ΡΡΠ΅Π½ ΠΏΡΠΎΡΠ΅ΡΡ ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° ΡΡΠΆΠ΅Π»ΠΎΠΉ Π½Π΅ΡΡΠΈ Π² ΠΏΡΠΈΡΡΡΡΡΠ²ΠΈΠΈ
ΡΠ΅ΠΎΠ»ΠΈΡΠ° Y, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠ΅Π³ΠΎ Π½Π°Π½ΠΎΡΠ°Π·ΠΌΠ΅ΡΠ½ΡΠΉ ΠΏΠΎΡΠΎΡΠΎΠΊ Π½ΠΈΠΊΠ΅Π»Ρ, ΠΏΡΠΈ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ΅ 450 Β°Π‘, Π΄Π°Π²Π»Π΅Π½ΠΈΠΈ
0,5β¦0,7 ΠΠΠ° ΠΈ ΠΏΡΠΎΠ΄ΠΎΠ»ΠΆΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΠΈ ΡΠ΅Π°ΠΊΡΠΈΠΈ 60 ΠΈ 120 ΠΌΠΈΠ½. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΡΠΎ Π½Π°ΠΈΠ±ΠΎΠ»ΡΡΠΈΠΉ
Π²ΡΡ
ΠΎΠ΄ ΡΡΠ°ΠΊΡΠΈΠΉ, Π²ΡΠΊΠΈΠΏΠ°ΡΡΠΈΡ
Π΄ΠΎ 350 Β°Π‘, Π½Π°Π±Π»ΡΠ΄Π°Π΅ΡΡΡ ΠΏΡΠΈ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π΅ Π½Π΅ΡΡΠΈ Ρ Π΄ΠΎΠ±Π°Π²ΠΊΠΎΠΉ
5,0 % ΠΌΠ°Ρ. ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠ° 2,0 % Ni/HY Π² ΡΠ΅ΡΠ΅Π½ΠΈΠ΅ 60 ΠΌΠΈΠ½ ΠΈ ΡΠΎΡΡΠ°Π²Π»ΡΠ΅Ρ 67,1 %. ΠΡΠΈΠ²ΠΎΠ΄ΡΡΡΡ
Π΄Π°Π½Π½ΡΠ΅ ΡΠΏΠ΅ΠΊΡΡΠΎΠΌΠ΅ΡΡΠΈΠΈ Π―ΠΠ 1Π, Π³ΡΡΠΏΠΏΠΎΠ²ΠΎΠ³ΠΎ ΠΈ Π²Π΅ΡΠ΅ΡΡΠ²Π΅Π½Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ²
ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° ΡΡΠΆΠ΅Π»ΠΎΠΉ Π½Π΅ΡΡΠΈ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ Π² ΠΆΠΈΠ΄ΠΊΠΎΠΌ
ΠΏΡΠΎΠ΄ΡΠΊΡΠ΅ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° Π½Π΅ΡΡΠΈ Ρ Π΄ΠΎΠ±Π°Π²ΠΊΠΎΠΉ 2,0 % Ni/HY ΡΠΎΠ΄Π΅ΡΠΆΠΈΡΡΡ ΠΌΠ΅Π½ΡΡΠ΅
ΡΠΌΠΎΠ» ΠΈ Π°ΡΡΠ°Π»ΡΡΠ΅Π½ΠΎΠ² ΠΈ Π±ΠΎΠ»ΡΡΠ΅ ΠΌΠ°ΡΠ΅Π» ΠΏΠΎ ΡΡΠ°Π²Π½Π΅Π½ΠΈΡ Ρ ΠΆΠΈΠ΄ΠΊΠΈΠΌΠΈ ΠΏΡΠΎΠ΄ΡΠΊΡΠ°ΠΌΠΈ ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ
ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° Π² ΠΏΡΠΈΡΡΡΡΡΠ²ΠΈΠΈ HY.Process of thermal and catalytic cracking of heavy oil at presence of zeolite Y containing nickel
nanopowder is studied at temperature 450 Β°Π‘, pressure 0,5 β¦ 0,7 ΠΠΠ° and durations of reaction 60
and 120 minutes It is shown, that the greatest yield of the distillate fractions boiling up to 350 Β°Π‘ is
obtained via crude oil catalytic cracking by an addition of 5 % mas. catalyst 2,0 % Ni/HY during of
experiment of 60 min, it is 67,1 %. Data of spectrometry of a nuclear magnetic resonance Π1, group
and material constitution of products of thermal and catalytic cracking of heavy oil are cited. It is
shown, that liquid product of catalytic cracking of heavy oil with the additive of 2,0 % Ni/HY contained
the least quantity of resins and asphaltenes and grater quantity of oils in comparison with liquid
products of thermal and catalytic cracking by addition catalyst HY
Cracking of Heavy Oil at Presence of Zeolite Y Modified of Nickel Nanopowder
ΠΠ·ΡΡΠ΅Π½ ΠΏΡΠΎΡΠ΅ΡΡ ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° ΡΡΠΆΠ΅Π»ΠΎΠΉ Π½Π΅ΡΡΠΈ Π² ΠΏΡΠΈΡΡΡΡΡΠ²ΠΈΠΈ
ΡΠ΅ΠΎΠ»ΠΈΡΠ° Y, ΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠ΅Π³ΠΎ Π½Π°Π½ΠΎΡΠ°Π·ΠΌΠ΅ΡΠ½ΡΠΉ ΠΏΠΎΡΠΎΡΠΎΠΊ Π½ΠΈΠΊΠ΅Π»Ρ, ΠΏΡΠΈ ΡΠ΅ΠΌΠΏΠ΅ΡΠ°ΡΡΡΠ΅ 450 Β°Π‘, Π΄Π°Π²Π»Π΅Π½ΠΈΠΈ
0,5β¦0,7 ΠΠΠ° ΠΈ ΠΏΡΠΎΠ΄ΠΎΠ»ΠΆΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΠΈ ΡΠ΅Π°ΠΊΡΠΈΠΈ 60 ΠΈ 120 ΠΌΠΈΠ½. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΡΠΎ Π½Π°ΠΈΠ±ΠΎΠ»ΡΡΠΈΠΉ
Π²ΡΡ
ΠΎΠ΄ ΡΡΠ°ΠΊΡΠΈΠΉ, Π²ΡΠΊΠΈΠΏΠ°ΡΡΠΈΡ
Π΄ΠΎ 350 Β°Π‘, Π½Π°Π±Π»ΡΠ΄Π°Π΅ΡΡΡ ΠΏΡΠΈ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π΅ Π½Π΅ΡΡΠΈ Ρ Π΄ΠΎΠ±Π°Π²ΠΊΠΎΠΉ
5,0 % ΠΌΠ°Ρ. ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠ° 2,0 % Ni/HY Π² ΡΠ΅ΡΠ΅Π½ΠΈΠ΅ 60 ΠΌΠΈΠ½ ΠΈ ΡΠΎΡΡΠ°Π²Π»ΡΠ΅Ρ 67,1 %. ΠΡΠΈΠ²ΠΎΠ΄ΡΡΡΡ
Π΄Π°Π½Π½ΡΠ΅ ΡΠΏΠ΅ΠΊΡΡΠΎΠΌΠ΅ΡΡΠΈΠΈ Π―ΠΠ 1Π, Π³ΡΡΠΏΠΏΠΎΠ²ΠΎΠ³ΠΎ ΠΈ Π²Π΅ΡΠ΅ΡΡΠ²Π΅Π½Π½ΠΎΠ³ΠΎ ΡΠΎΡΡΠ°Π²Π° ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ²
ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° ΡΡΠΆΠ΅Π»ΠΎΠΉ Π½Π΅ΡΡΠΈ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ, ΡΡΠΎ Π² ΠΆΠΈΠ΄ΠΊΠΎΠΌ
ΠΏΡΠΎΠ΄ΡΠΊΡΠ΅ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° Π½Π΅ΡΡΠΈ Ρ Π΄ΠΎΠ±Π°Π²ΠΊΠΎΠΉ 2,0 % Ni/HY ΡΠΎΠ΄Π΅ΡΠΆΠΈΡΡΡ ΠΌΠ΅Π½ΡΡΠ΅
ΡΠΌΠΎΠ» ΠΈ Π°ΡΡΠ°Π»ΡΡΠ΅Π½ΠΎΠ² ΠΈ Π±ΠΎΠ»ΡΡΠ΅ ΠΌΠ°ΡΠ΅Π» ΠΏΠΎ ΡΡΠ°Π²Π½Π΅Π½ΠΈΡ Ρ ΠΆΠΈΠ΄ΠΊΠΈΠΌΠΈ ΠΏΡΠΎΠ΄ΡΠΊΡΠ°ΠΌΠΈ ΡΠ΅ΡΠΌΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΈ
ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΎΠ³ΠΎ ΠΊΡΠ΅ΠΊΠΈΠ½Π³Π° Π² ΠΏΡΠΈΡΡΡΡΡΠ²ΠΈΠΈ HY.Process of thermal and catalytic cracking of heavy oil at presence of zeolite Y containing nickel
nanopowder is studied at temperature 450 Β°Π‘, pressure 0,5 β¦ 0,7 ΠΠΠ° and durations of reaction 60
and 120 minutes It is shown, that the greatest yield of the distillate fractions boiling up to 350 Β°Π‘ is
obtained via crude oil catalytic cracking by an addition of 5 % mas. catalyst 2,0 % Ni/HY during of
experiment of 60 min, it is 67,1 %. Data of spectrometry of a nuclear magnetic resonance Π1, group
and material constitution of products of thermal and catalytic cracking of heavy oil are cited. It is
shown, that liquid product of catalytic cracking of heavy oil with the additive of 2,0 % Ni/HY contained
the least quantity of resins and asphaltenes and grater quantity of oils in comparison with liquid
products of thermal and catalytic cracking by addition catalyst HY