In order to improve the propylene selectivity and activity stability in methanol to olefins(MTO)reaction,the effects of element modification and composite modification on the acidity and activity of HZSM-5 zeolite catalyst were studiedBoron modificationAt SiO2/Al2O3?400 and B/Al=1,the acid strength of BHZSM-5 retained unchanged compared with that of HZSM-5.The weak Br(?)nsted(B)acid amount was increased whereas the strong B acid amount decreased by 50%and the total acid amount increased.The propylene selectivity rose by 4%.The hydrogen transfer reaction was suppressed and the activity durability improved.Subjected to hydrothermal circumstances,more acid amount of BHZSM-5 maintained.The framework A1 in the straight and sinusoidal channels was not easy to remove compared with those in the channel intersections,which is conducive to the alkene-based cycle mechanism.The propylene selectivity reached 37.4%.At SiO2/Al2O3?400 and B/Al=1,9,the weak B acid amount was increased by 1 times whereas the amount strong B acid remained.The activity durability BHZSM-5-4000-9 extended for 50 h.ZSM-11 cocrystallization compositeZSM-5/ZSM-l1 zeolite was synthesized using hydrothermal cocrystallization.The charging SiO2/Al2O3 ratio was 180 and the ZSM-11 content was 15%.The cocrystal zeolite showed similar crystallinity,morphology,porosity,weak and medium strong B acid amount as HZSM-5,but more strong B acid amount.The propylene selectivity was raised by 10%.The A1 in the straight channels was increased,beneficial to the formation of propylene via the alkene-based cycle mechanism.SAPO-n compositeSAPO-11(SiO2/Al2O3=0.2)was composited with HZSM-5(SiO2/Al2O3=160)using hydrothermal crystallization.The propylene selectivity was improved.With increase of the HZSM-5/SAPO-11 ratio from 0.65 to 1.08,the strong acid amount was decreased by 61%.When the ratio was 1.08,the propylene and ethylene selectivity was 27.6%and 43.8%,respectively,and the C5+ selectivity 9.1%,relating to enhanced cracking.SAPO-18(SiO2/Al2O3=0.2)was composited with HZSM-5 in the ratio of 1.22.The strong acid amount was markedly increased.With further strengthened cracking,propylene was increased up to 42.5%and C5+ reduced to 8.6%.The activity stabilized for 64 h. |