A kind of reaction separation bifunctional catalytic membrane reaction device for catalyzing methanol dehydration to prepare dimethyl ether and its application
A technology of dual-functional catalysis and reaction device, which is applied in the dehydration of hydroxyl-containing compounds to prepare ethers, chemical/physical/physical-chemical fixed reactors, ether preparations, etc., which can solve the problem of dual-functional coupling and single reaction that cannot be satisfied at the same time. or issues like separating functions
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Embodiment 1
[0124] Embodiment 1FAU-LTA molecular sieve membrane catalytic reactor 1
[0125] making process
[0126] Step 1. Functional modification of porous matrix
[0127] The substrates of synthetic molecular sieve membranes such as porous alumina ceramics, porous titania ceramics, porous stainless steel and stainless steel mesh were respectively placed in 0.2 mol / L organic solvents such as APTES, DICB, CPTMS, CPTCS, CPDMS, CPCS, BPTMS, BPPCS and IPTMS. In the toluene solution of silane, react at 110°C for 0.5~3h, so as to introduce -NH on the surface of the substrate 2 , -NCO, -Cl, -Br and -I and other organic functional groups to form a functionally modified porous matrix for molecular sieve membrane synthesis.
[0128] Step 2, prepare the synthetic solution of molecular sieve membrane
[0129] Weigh a certain amount of NaOH and dissolve it in distilled water, add aluminum foil after clarification, and stir to form an aluminum solution; measure a certain amount of silica sol and ...
Embodiment 2
[0148] Embodiment 2FAU-LTA molecular sieve membrane catalytic reactor 2
[0149] The preparation process is the same as in Example 1, except that the ion exchange time in step 6 is 36 hours.
[0150] The performance testing process is the same as that in Example 1, except that the raw material flow rate is 0.20 g / h.
Embodiment 3
[0151] Embodiment 3FAU-LTA molecular sieve membrane catalytic reactor 3
[0152] The preparation process is the same as in Example 1, except that the ion exchange time in step 6 is 48 hours.
[0153] The performance testing process is the same as in Example 1, except that the flow rate of the raw material is 0.25 g / h, and the long-term stability of the catalyst is tested at 280°C.
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