FIELD: chemistry.
SUBSTANCE: present invention relates to a method for producing an additive, including the stages of: a) obtaining a suspension of clay and aluminium oxide: i) dispersing kaolin clay in demineralised water and a dispersing agent, wherein said dispersing agent constitutes a naphtalenesulfonic acid condensation product; ii) adding a pseudoboehmite-type aluminium oxide; iii) grinding the suspension for 2 hours, mixing homogeneously, and then adding ammonium polysilicate and grinding again for at least 30 minutes; and iv) gradually adding an organic acid followed by adding phosphoric acid while thoroughly mixing; b) obtaining a zeolite suspension using more than one zeolite: i) dissolving diammonium hydrogen phosphate in demineralised water to produce a zeolite suspension; adding a ZSM-5 zeolite with SiO2/Al2O3 in the range from 30 to 280 to the demineralised water while mixing; and ii) dissolving the diammonium hydrogen phosphate in demineralised water to obtain a zeolite suspension; adding a ZSM-5 zeolite with SiO2/Al2O3 to the demineralised water while mixing; wherein the molar ratio of SiO2/Al2O3 is different from stage (i); c) obtaining a finished catalytic suspension: i) mixing the zeolite suspension with a suspension of clay and aluminium oxide and stirring for 30 minutes; ii) adding ammonium polysilicate to the suspension mixed in stage i) of stage c), and optionally adding a divalent metal precursor dissolved in demineralised water; and iii) screening the suspension obtained in stage ii) of stage c), spray drying and calcinating the spray-dried product at a temperature of 550°C. The invention also relates to a composition of a fluid-catalytic cracking additive obtained by the above method, wherein said composition of the fluid-catalytic cracking additive is configured to increase the octane number of gasoline.
EFFECT: optimising a typical combination of an MFI-type zeolite with different ratio of SiO2/Al2O3 to maintain the output of gasoline and increase the octane number of gasoline, leading to increasing the selectivity by light olefins and aromatic compounds in the product; in the modification of acidic centres of the additive using divalent metal selected from the Group IIA and Group IB to ensure the selectivity by light olefins and aromatic compounds.
8 cl, 3 tbl, 9 ex
| Title | Year | Author | Number | 
|---|---|---|---|
| METHOD OF CRACKING AND PERFECTED CATALYSTS TO THIS END | 2009 | 
 | RU2497589C2 | 
| CATALYST FOR PROCESSING GASOLINE FRACTIONS | 2024 | 
 | RU2830363C1 | 
| PHOSPHORUS-CONTAINING FCC CATALYST | 2014 | 
 | RU2683034C1 | 
| CATALYST COMPOSITION FOR PROCESSING HEAVY STARTING MATERIAL | 2007 | 
 | RU2427424C2 | 
| FCC CATALYST COMPOSITIONS CONTAINING BORON OXIDE AND PHOSPHORUS | 2014 | 
 | RU2684613C1 | 
| FCC CATALYST COMPOSITIONS CONTAINING BORON OXIDE | 2014 | 
 | RU2696280C1 | 
| CATALYST REDUCING THE CONCENTRATION OF SULPHUR IN BENZINES USED IN THE METHOD OF CATALYTICAL CRACKING IN THE CATALYST FLUIDISED LAYER | 2008 | 
 | RU2442649C2 | 
| CATALYST FOR CATALYTIC CRACKING OF HYDROCARBON, USED IN OBTAINING LIGHT OLEFIN, AND METHOD OF OBTAINING THEREOF | 2009 | 
 | RU2494809C2 | 
| ZSM-5 ADDITIVE ACTIVITY ENHANCEMENT BY IMPROVED ZEOLITE AND PHOSPHORUS INTERACTION | 2014 | 
 | RU2672919C2 | 
| BORON OXIDE IN FCC PROCESSES | 2014 | 
 | RU2678446C1 | 
Authors
Dates
2021-08-30—Published
2020-10-02—Filed