The invention relates to a ZSM-5 / beta
zeolite / MCM-49 triphase coexisting
molecular sieve and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single in pore-size, weak in acid and low in activity. The method prepares the ZSM-5 / beta
zeolite / MCM-49 triphase coexisting
molecular sieve by adding a
seed crystal containing an MCM-49 precursor during a synthesis process of diphase coexisting
molecular sieve. A mole relation of the components of the synthesized triphase coexisting molecular
sieve is nSiO2 :Al2O3, wherein n is between 10 and 1,000; the triphase coexisting molecular
sieve has more than three phases; the XRD
diffraction pattern of the triphase coexisting molecular
sieve comprises a technical proposal that a maximum value of a distance d is at positions between 12.26-0.1 and 12.26+0.1 A, 11.32-0.04 and 11.32+0.04 A, 11.22-0.04 and 11.22+0.04 A, 11.08-0.05 and 11.08+0.05 A, 9.97-0.1 and 9.97+0.1 A, 8.82-0.1 and 8.82+0.1 A, 7.74-0.1 and 7.74+0.1 A,6.14-0.1 and 6.14+0.1 A, 5.14-0.1 and 5.14+0.1 A, 4.15-0.1 and 4.15+0.1 A, 3.90-0.05 and 3.90+0.05 A,3.71-0.1 and 3.71+0.1 A,3.45-0.05 and 3.45+0.05,3.29-0.04 and 3.29+0.04 A ,3.20-0.04 and 3.29+0.04 A ,3.08-0.04 and 3.08+0.04 A, and 2.98-0.05 and 2.98+0.05 A; therefore, the problems are solved well. The triphase coexisting molecular sieve can be used in the industrial production of
ethylene and propylene through the
catalytic pyrolysis of
naphtha.