Continuous reaction and regeneration technology used for conversion of methanol to gasoline through stationary bed adiabatic reactors
An adiabatic reactor, methanol conversion technology, which is applied in the petroleum industry, bulk chemical production, biological raw materials, etc., can solve the problem of "the remaining activity of the catalyst is difficult to use, etc., and achieve the improvement of the effective utilization rate, the reduction of energy consumption, and the reduction of raw material waste. Effect
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Embodiment 1
[0060] Two fixed-bed adiabatic reactors are attached by several pipes and valves. figure 1 Process connections shown.
[0061] R-a and R-b are fixed-bed adiabatic reactors made of stainless steel with an inner diameter of 3200 mm. The two reactors are respectively equipped with 23.29 tons of FeZrZSM-5 molecular sieve catalyst manufactured according to the method disclosed in Chinese Patent ZL200610012810.4, and the net height of the catalyst bed is 4830 mm. The total loading of FeZrZSM-5 molecular sieve catalyst in the two reactors is 46.58 tons.
[0062] The whole system was purged with nitrogen, and the oxygen content was confirmed to be less than 0.5%, and the system pressure was controlled at 1.8MPa.
[0063] Valves 3a, 7a are open and valves 3b, 7b, 10a, 10b, 12a, 12b, 14a, 14b, 15a, 15b are closed.
[0064] The system nitrogen circulation is established through the external circulation system, and the nitrogen flow rate entering the fixed-bed adiabatic reactor R-a thr...
Embodiment 2
[0102] The catalyst loading conditions and operating conditions are completely the same as those in Example 1, but the catalyst adopts ZSM-5 molecular sieve catalyst.
[0103] The main parameters of Example 2 are shown in Table 3.
[0104] The main technical indicators of Example 2 are shown in Table 4.
Embodiment 3
[0114] Same as Example 1, but the catalyst adopts ZSM-12 molecular sieve catalyst.
[0115] The main parameters of Example 3 are shown in Table 5.
[0116] The main technical indicators of Example 3 are shown in Table 6.
[0117] Table 5 Main parameters of Example 3
[0118] project
[0119] Table 6 Main technical indicators of embodiment 3
[0120] project
[0121] Number of reactors switched for regeneration per year
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