2 research outputs found
ΠΠ»ΠΈΡΠ½ΠΈΠ΅ ΡΠ΅Π»ΠΎΡΠ½ΠΎΠΉ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠΈ Π½Π° ΡΠΈΠ·ΠΈΠΊΠΎ-Ρ ΠΈΠΌΠΈΡΠ΅ΡΠΊΠΈΠ΅ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΈΠ΅ ΡΠ²ΠΎΠΉΡΡΠ²Π° ΡΠ΅ΠΎΠ»ΠΈΡΠ° ΡΠΈΠΏΠ° ZSMβ5 Π² ΠΏΡΠΎΡΠ΅ΡΡΠ΅ ΠΏΡΠ΅Π²ΡΠ°ΡΠ΅Π½ΠΈΡ ΠΏΡΡΠΌΠΎΠ³ΠΎΠ½Π½ΠΎΠΉ Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ²ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ Π½Π΅ΡΡΠΈ
Postsynthetic treatment of a ZSMβ5 type zeolite with aqueous solutions of NaOH of various concentrations is carried out. Structural, acidic, and catalytic properties of the initial zeolite and treated samples are investigated in the course of conversion of straight-run gasoline fraction of oil. The main operational characteristics of the obtained high-octane gasolines are determined. The dynamics of deactivation of the initial ZSMβ5 zeolite and the sample subjected to alkaline treatment is reported and the structure of coke deposits is studied. It is found out that alkaline treatment of zeolites leads to a decrease in their crystallinity, specific surface area and specific mesopore volume, while the average pore diameter increases. Also a decrease in the concentration of acid sites with an increase in their strength is observed. As a result of changes in the properties of zeolites, the performance and stability of the catalysts obtained on their basis increase, which contributes to the improvement of the quality of gasoline formed over these catalysts during the conversion of straight-run gasoline fraction of oilΠΡΠΎΠ²Π΅Π΄Π΅Π½Π° ΠΏΠΎΡΡΡΠΈΠ½ΡΠ΅ΡΠΈΡΠ΅ΡΠΊΠ°Ρ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠ° ΡΠ΅ΠΎΠ»ΠΈΡΠ° ΡΠΈΠΏΠ° ZSMβ5 Π²ΠΎΠ΄Π½ΡΠΌΠΈ ΡΠ°ΡΡΠ²ΠΎΡΠ°ΠΌΠΈ
NaOH ΡΠ°Π·Π»ΠΈΡΠ½ΠΎΠΉ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΈΠΈ. ΠΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½Ρ ΡΡΡΡΠΊΡΡΡΠ½ΡΠ΅, ΠΊΠΈΡΠ»ΠΎΡΠ½ΡΠ΅ ΠΈ ΠΊΠ°ΡΠ°Π»ΠΈΡΠΈΡΠ΅ΡΠΊΠΈΠ΅
ΡΠ²ΠΎΠΉΡΡΠ²Π°
ΠΈΡΡ
ΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠ΅ΠΎΠ»ΠΈΡΠ° ΠΈ ΠΎΠ±ΡΠ°Π±ΠΎΡΠ°Π½Π½ΡΡ
ΠΎΠ±ΡΠ°Π·ΡΠΎΠ² Π² ΠΏΡΠΎΡΠ΅ΡΡΠ΅ ΠΏΡΠ΅Π²ΡΠ°ΡΠ΅Π½ΠΈΡ ΠΏΡΡΠΌΠΎΠ³ΠΎΠ½Π½ΠΎΠΉ
Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ²ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ Π½Π΅ΡΡΠΈ. ΠΠΏΡΠ΅Π΄Π΅Π»Π΅Π½Ρ ΠΎΡΠ½ΠΎΠ²Π½ΡΠ΅ ΡΠΊΡΠΏΠ»ΡΠ°ΡΠ°ΡΠΈΠΎΠ½Π½ΡΠ΅ Ρ
Π°ΡΠ°ΠΊΡΠ΅ΡΠΈΡΡΠΈΠΊΠΈ ΠΏΠΎΠ»ΡΡΠ΅Π½Π½ΡΡ
Π²ΡΡΠΎΠΊΠΎΠΎΠΊΡΠ°Π½ΠΎΠ²ΡΡ
Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ². ΠΡΠΈΠ²Π΅Π΄Π΅Π½Π° Π΄ΠΈΠ½Π°ΠΌΠΈΠΊΠ° Π΄Π΅Π·Π°ΠΊΡΠΈΠ²Π°ΡΠΈΠΈ ΠΈΡΡ
ΠΎΠ΄Π½ΠΎΠ³ΠΎ ΡΠ΅ΠΎΠ»ΠΈΡΠ° ZSMβ5
ΠΈ ΠΎΠ±ΡΠ°Π·ΡΠ°, ΠΏΠΎΠ΄Π²Π΅ΡΠ³Π½ΡΡΠΎΠ³ΠΎ ΡΠ΅Π»ΠΎΡΠ½ΠΎΠΉ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠ΅, ΠΈΠ·ΡΡΠ΅Π½Π° ΡΡΡΡΠΊΡΡΡΠ° ΠΊΠΎΠΊΡΠΎΠ²ΡΡ
ΠΎΡΠ»ΠΎΠΆΠ΅Π½ΠΈΠΉ.
Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ, ΡΡΠΎ ΡΠ΅Π»ΠΎΡΠ½Π°Ρ ΠΎΠ±ΡΠ°Π±ΠΎΡΠΊΠ° ΡΠ΅ΠΎΠ»ΠΈΡΠΎΠ² ΠΏΡΠΈΠ²ΠΎΠ΄ΠΈΡ ΠΊ ΡΠ½ΠΈΠΆΠ΅Π½ΠΈΡ ΠΈΡ
ΠΊΡΠΈΡΡΠ°Π»Π»ΠΈΡΠ½ΠΎΡΡΠΈ,
Π²Π΅Π»ΠΈΡΠΈΠ½Ρ ΡΠ΄Π΅Π»ΡΠ½ΠΎΠΉ ΠΏΠΎΠ²Π΅ΡΡ
Π½ΠΎΡΡΠΈ ΠΈ ΡΠ΄Π΅Π»ΡΠ½ΠΎΠ³ΠΎ ΠΎΠ±ΡΡΠΌΠ° ΠΌΠ΅Π·ΠΎΠΏΠΎΡ, ΡΠ²Π΅Π»ΠΈΡΠ΅Π½ΠΈΡ ΡΡΠ΅Π΄Π½Π΅Π³ΠΎ Π΄ΠΈΠ°ΠΌΠ΅ΡΡΠ°
ΠΏΠΎΡ, ΡΠΌΠ΅Π½ΡΡΠ΅Π½ΠΈΡ ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΈΠΈ ΠΊΠΈΡΠ»ΠΎΡΠ½ΡΡ
ΡΠ΅Π½ΡΡΠΎΠ² ΠΈ ΡΠ²Π΅Π»ΠΈΡΠ΅Π½ΠΈΡ ΠΈΡ
ΡΠΈΠ»Ρ. Π ΡΠ΅Π·ΡΠ»ΡΡΠ°ΡΠ΅
ΠΏΡΠΎΠΈΡΡ
ΠΎΠ΄ΡΡΠΈΡ
ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠΉ ΡΠ²ΠΎΠΉΡΡΠ²
ΡΠ΅ΠΎΠ»ΠΈΡΠΎΠ² ΠΏΠΎΠ²ΡΡΠ°Π΅ΡΡΡ ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΡ ΠΈ ΡΡΠ°Π±ΠΈΠ»ΡΠ½ΠΎΡΡΡ
ΡΠ°Π±ΠΎΡΡ ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠΎΠ², ΠΏΠΎΠ»ΡΡΠ΅Π½Π½ΡΡ
Π½Π° ΠΈΡ
ΠΎΡΠ½ΠΎΠ²Π΅, Π° ΡΠ°ΠΊΠΆΠ΅ ΡΠ»ΡΡΡΠ°Π΅ΡΡΡ ΠΊΠ°ΡΠ΅ΡΡΠ²ΠΎ Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ²,
ΠΎΠ±ΡΠ°Π·ΡΡΡΠΈΡ
ΡΡ Π½Π° Π½ΠΈΡ
Π² ΠΏΡΠΎΡΠ΅ΡΡΠ΅ ΠΏΡΠ΅Π²ΡΠ°ΡΠ΅Π½ΠΈΡ ΠΏΡΡΠΌΠΎΠ³ΠΎΠ½Π½ΠΎΠΉ Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ²ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ Π½Π΅ΡΡ
Physicochemical and Catalytic Properties of Rhenium-Containing Zeolites in the Course of Straight-Run Gasoline Upgrading
ΠΠ° ΠΎΡΠ½ΠΎΠ²Π΅ ΡΠ΅ΠΎΠ»ΠΈΡΠ° ΡΡΡΡΠΊΡΡΡΠ½ΠΎΠ³ΠΎ ΡΠΈΠΏΠ° ZSMβ5 ΡΡΡ
ΠΈΠΌ ΠΌΠ΅Ρ
Π°Π½ΠΈΡΠ΅ΡΠΊΠΈΠΌ ΡΠΌΠ΅ΡΠ΅Π½ΠΈΠ΅ΠΌ
Ρ ΡΠ»ΡΡΡΠ°Π΄ΠΈΡΠΏΠ΅ΡΡΠ½ΡΠΌ ΠΏΠΎΡΠΎΡΠΊΠΎΠΌ ΡΠ΅Π½ΠΈΡ ΠΏΠΎΠ»ΡΡΠ΅Π½Ρ ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΡ Π΄Π»Ρ ΠΎΠ±Π»Π°Π³ΠΎΡΠ°ΠΆΠΈΠ²Π°Π½ΠΈΡ ΠΏΡΡΠΌΠΎΠ³ΠΎΠ½Π½ΠΎΠΉ
Π±Π΅Π½Π·ΠΈΠ½ΠΎΠ²ΠΎΠΉ ΡΡΠ°ΠΊΡΠΈΠΈ Π½Π΅ΡΡΠΈ. ΠΠΎΠΊΠ°Π·Π°Π½ΠΎ ΠΈΠ·ΠΌΠ΅Π½Π΅Π½ΠΈΠ΅ ΡΡΡΡΠΊΡΡΡΠ½ΡΡ
ΠΈ ΠΊΠΈΡΠ»ΠΎΡΠ½ΡΡ
Ρ
Π°ΡΠ°ΠΊΡΠ΅ΡΠΈΡΡΠΈΠΊ
ΡΠ΅ΠΎΠ»ΠΈΡΠ° ZSMβ5 ΠΏΡΠΈ Π΅Π³ΠΎ ΠΌΠΎΠ΄ΠΈΡΠΈΡΠΈΡΠΎΠ²Π°Π½ΠΈΠΈ ΡΠ΅Π½ΠΈΠ΅ΠΌ. ΠΠΏΡΠ΅Π΄Π΅Π»Π΅Π½Π° ΠΊΠΎΠ½ΡΠ΅Π½ΡΡΠ°ΡΠΈΡ ΠΈ ΠΏΡΠΈΡΠΎΠ΄Π°
ΡΠ³Π»Π΅ΡΠΎΠ΄Π½ΡΡ
ΠΏΡΠΎΠ΄ΡΠΊΡΠΎΠ² ΡΠΏΠ»ΠΎΡΠ½Π΅Π½ΠΈΡ, ΠΎΠ±ΡΠ°Π·ΡΡΡΠΈΡ
ΡΡ Π½Π° ΠΏΠΎΠ»ΡΡΠ΅Π½Π½ΡΡ
ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠ°Ρ
ΠΏΡΠΈ ΠΏΠ΅ΡΠ΅ΡΠ°Π±ΠΎΡΠΊΠ΅
ΠΏΡΡΠΌΠΎΠ³ΠΎΠ½Π½ΠΎΠ³ΠΎ Π±Π΅Π½Π·ΠΈΠ½Π°. Π£ΡΡΠ°Π½ΠΎΠ²Π»Π΅Π½ΠΎ ΠΏΠΎΠ²ΡΡΠ΅Π½ΠΈΠ΅ ΡΡΡΠ΅ΠΊΡΠΈΠ²Π½ΠΎΡΡΠΈ ΡΠ°Π±ΠΎΡΡ ΡΠ΅Π½ΠΈΠΉΡΠΎΠ΄Π΅ΡΠΆΠ°ΡΠΈΡ
ΡΠ΅ΠΎΠ»ΠΈΡΠ½ΡΡ
ΠΊΠ°ΡΠ°Π»ΠΈΠ·Π°ΡΠΎΡΠΎΠ² ΠΏΠΎ ΡΡΠ°Π²Π½Π΅Π½ΠΈΡ Ρ Π½Π΅ΠΌΠΎΠ΄ΠΈΡΠΈΡΠΈΡΠΎΠ²Π°Π½Π½ΡΠΌ ΡΠ΅ΠΎΠ»ΠΈΡΠΎΠΌ, Π·Π°ΠΊΠ»ΡΡΠ°ΡΡΠ΅Π΅ΡΡ
Π² ΡΠ²Π΅Π»ΠΈΡΠ΅Π½ΠΈΠΈ ΠΈΡ
ΠΏΡΠΎΠΈΠ·Π²ΠΎΠ΄ΠΈΡΠ΅Π»ΡΠ½ΠΎΡΡΠΈ ΠΈ ΡΠ½ΠΈΠΆΠ΅Π½ΠΈΠΈ ΡΠΊΠΎΡΠΎΡΡΠΈ Π΄Π΅Π·Π°ΠΊΡΠΈΠ²Π°ΡΠΈΠΈ Π² ΠΈΡΡΠ»Π΅Π΄ΠΎΠ²Π°Π½Π½ΠΎΠΌ
ΠΏΡΠΎΡΠ΅ΡΡΠ΅Catalysts for upgrading of the straight-run gasoline fraction of oil were prepared on the basis of a ZSMβ5 zeolite via dry mechanical mixing with an ultrafine rhenium powder. It was shown how the structural and acidic characteristics of zeolite ZSMβ5 changed when it was modified with rhenium. The concentration and nature of carbon condensation products formed on the prepared catalysts during the processing of straight--run gasoline have been determined. An enhancement of operating efficiency of rhenium--containing zeolite catalysts in comparison with an unmodified zeolite was established, which consisted in increasing their capacity and reducing the rate of deactivation in the process under stud