Method for preparing vinyl monomers and vinyl chloride monomers
A technology of vinyl chloride monomer and ethylene, applied in the field of joint preparation of ethylene and vinyl chloride monomer, can solve the problems of high pollution, high energy consumption, etc., and achieve the effect of high flexibility, clean production process and environmental protection
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Embodiment 1
[0036] After dissolving a certain mass of precursors of barium, tungsten, cerium and potassium in water, adding silicon-aluminum molecular sieves and stirring evenly, drying and roasting to obtain a catalyst, the molar ratio of methane, methyl chloride and oxygen is 1:0.01:0.2 After mixing, it is passed into the reactor, the reaction temperature is 900°C, and the reaction pressure is normal pressure. The reaction effluent is washed with water and alkali to remove hydrogen chloride, condensed to remove water, and the composition is analyzed. The conversion rate of methane and methyl chloride is calculated according to the carbon balance before and after the reaction. Ethylene and vinyl chloride selectivities were calculated using carbon product normalization. The one-pass conversion rate of methane can reach 45%, all the methyl chloride can be converted, the selectivity of ethylene can reach 50%, and no vinyl chloride is detected.
Embodiment 2
[0038] After dissolving a certain mass of precursors of barium, tungsten, cerium and potassium in water, adding silicon-aluminum molecular sieves and stirring evenly, drying and roasting to obtain a catalyst, the molar ratio of methane, methyl chloride and oxygen is 1:0.5:0.4 After mixing, it is passed into the reactor, the reaction temperature is 800°C, and the reaction pressure is normal pressure. The reaction effluent is washed with water and alkali to remove hydrogen chloride, condensed to remove water, and the composition is analyzed. The conversion rate of methane and methyl chloride is calculated according to the carbon balance before and after the reaction. Ethylene and vinyl chloride selectivities were calculated using carbon product normalization. The single-pass conversion rate of methane is about 40%, the single-pass conversion rate of methyl chloride is 75%, the selectivity of ethylene is 45%, and the selectivity of vinyl chloride is 28%.
Embodiment 3
[0040] After dissolving a certain mass of precursors of barium, tungsten, cerium and potassium in water, adding silicon-aluminum molecular sieves and stirring evenly, drying and roasting to obtain a catalyst, the molar ratio of methane, methyl chloride and oxygen is 1:1:1 After mixing, it is passed into the reactor, the reaction temperature is 700°C, and the reaction pressure is normal pressure. The reaction effluent is washed with water and alkali to remove hydrogen chloride, condensed to remove water, and the composition is analyzed. The conversion rate of methane and methyl chloride is calculated according to the carbon balance before and after the reaction. Ethylene and vinyl chloride selectivities were calculated using carbon product normalization. The single-pass conversion rate of methane is 38%, the single-pass conversion rate of methyl chloride is 80%, the selectivity of ethylene is 25%, and the selectivity of vinyl chloride is 55%.
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