A kind of method that uses solid catalyst to carry out isopropyltoluene isomerization
A technology of isopropyltoluene and solid catalysts, which is applied in the direction of catalysts, molecular sieve catalysts, carbon compound catalysts, etc., can solve the problems of small pore size, harsh operating environment, and restrictions on the application of solid catalysts, and achieve convenient separation, simple post-processing, and overall Effect of High Atom Utilization
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Embodiment 1
[0026] Example 1 (HY molecular sieve)
[0027] Add 56g HY molecular sieve (SiO 2 / Al 2 O 3 = 5.3). The raw material is a mixture of o- and m-cymene added with toluene, wherein the mass fractions of m-cymene, o-cymene and toluene are respectively: 37%, 3% and 60%, and the feed flow rate is 1.63mL / min, converted to mass airspeed of 1.5h -1 . The reaction temperature was 340° C. and the pressure was 0.1 MPa. The compositions of the components in the obtained isomerization reaction solution were shown in Table 1. The product intermediate / para / ortho=64.1 / 30.4 / 5.4, the isomer distribution is close to thermodynamic equilibrium, the ortho- and meta-isopropyltoluene is converted to para-isopropyltoluene to the greatest extent, and the single-pass yield of para-isopropyltoluene is 18.3 %.
[0028] Yield of p-cymene in one pass = mass of p-cymene in the product / (mass of intermediate cymene in the raw material + mass of o-cymene in the raw material)*100%.
Embodiment 2
[0029] Example 2 (HY molecular sieve)
[0030] Add 56g HY molecular sieve (SiO 2 / Al 2 O 3 = 9.7). The raw material is a mixture of o- and m-cymene added with toluene, wherein the mass fractions of m-cymene, o-cymene and toluene are respectively: 37%, 3% and 60%, and the feed flow rate is 1.63mL / min, converted to mass airspeed of 1.5h -1 . The reaction temperature was 340° C. and the pressure was 0.1 MPa. The compositions of the components in the obtained isomerization reaction solution were shown in Table 1. The product intermediate / para / ortho=64.5 / 29.7 / 5.8, the isomer distribution is also basically close to the thermodynamic equilibrium, the ortho and meta cumene are converted to para-cumene to the greatest extent, and the ratio of silicon to aluminum ratio is increased. The activity decreased slightly, but the decomposition of cumene slowed down, and the single-pass yield increased slightly, and the single-pass yield of p-cymene was 20.5%.
Embodiment 3
[0031] Example 3 (HY molecular sieve)
[0032] Add 56g HY molecular sieve (SiO 2 / Al 2 O 3 = 14.2). The raw material is a mixture of o- and m-cymene added with toluene, wherein the mass fractions of m-cymene, o-cymene and toluene are respectively: 37%, 3% and 60%, and the feed flow rate is 1.63mL / min, converted to mass airspeed of 1.5h -1 . The reaction temperature was 340° C. and the pressure was 0.1 MPa. The compositions of the components in the obtained isomerization reaction solution were shown in Table 1. The intermediate / para / ortho=72.3 / 21.4 / 6.3 of the product, with the further increase of the silicon-alumina ratio, the activity is further weakened, and the thermodynamic equilibrium is not reached, but the decomposition of the raw material is also reduced, and the single-pass yield of p-Cumene is 15.2%.
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