Device and method for preparing durene by utilizing methyl alcohol and mixed C4
A technology of mesitylene and methanol, applied in the field of petrochemical product synthesis, can solve the problems of unsatisfactory catalyst activity, selectivity and stability, high cost of raw materials, limited source of raw materials, etc. The effect of less discharge of three wastes and less process by-products
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Embodiment 1
[0051] A device that utilizes methanol and mixed C4 to prepare durene, such as figure 1 As shown, it includes an alkylation reactor 1, an oil-water separator 2, a de-C5 rectification tower 3, a de-C9 rectification tower 4, an alkylation reactor 5 and a freeze crystallization device 6, and the alkylation reactor 1 is vertically arranged, The alkylation reactor 1 is divided into the first section, the second section and the third section from top to bottom, the top, the first section and the second section of the alkylation reactor 1 have methanol inlets, and the second section of the alkylation reactor 1 The mixed C4 inlet is opened in the first section, and the product outlet is opened at the bottom of the alkylation reactor 1. The first section is filled with H-ZSM-5 after hydrothermal treatment, the second section is filled with Ag modified H-ZSM-5, and the third section is filled with Filled with Ni modified H-ZSM-5;
[0052] Methanol and mixed C4 enter the alkylation reac...
Embodiment 2
[0056] This embodiment is the same as Embodiment 1, the difference is:
[0057] The molar ratio of methanol and mixed C4 feed is 3:1 (methanol is the total amount entering the alkylation reactor; the proportion of methanol entering the top of the reactor, the first section, and the second section is required to be 50%, 10%, and 40% ), the three-stage reaction conditions of the alkylation reactor: temperature 390°C, pressure 3MPa, mass space velocity 2h -1 , the residence time is 2s; the reaction conditions of the alkylation reactor: the reaction temperature is 380°C, the reaction pressure is 3.0MPa, and the mass space velocity is 2h -1 . The durene with a purity of 98% was obtained, and the yield of durene was 28%.
Embodiment 3
[0059] This embodiment is the same as Embodiment 1, the difference is:
[0060] The molar ratio of methanol and mixed C4 feed is 4:1, and the three-stage reaction conditions of the alkylation reactor are: temperature 400°C, pressure 4MPa, mass space velocity 3h -1 , the residence time is 4s; the reaction conditions of the alkylation reactor: the reaction temperature is 400°C, the reaction pressure is 4.0MPa, and the mass space velocity is 4h -1 . Freeze and crystallize at -15°C. After crystallization, centrifuge at 1500 r / min to obtain durene with a purity of 97%, and the yield of durene is 27%.
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