A preparation method, rectification equipment and treatment process of methyl oleate
A technology of methyl oleate and rectification, which is applied to the preparation of carboxylic acid esters, the preparation of organic compounds, chemical instruments and methods, etc., can solve the problems of unrealizable materials, low product yield, large amount of methanol consumption, etc., and achieve saving Effects of time and energy, increase in yield, and saving manpower and material resources
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Embodiment 1
[0028] Add 3.5 tons of acidified oil into the reaction kettle, and then add a solid acid catalyst H with an acidified oil quality of 5‰ 2 SO 4 / SiO 2 , stir and gradually raise the temperature to 95°C, then feed methanol for esterification reaction, the time for the first feed of methanol is 3 hours, the amount of methanol used is 3 tons, the mass ratio of acidified oil to methanol is 1.17:1 when the acid value drops to 2mg / g When the reaction ends, the liquid crude methyl ester is then added to the heating evaporator 1 for decomposition, and the gas-liquid mixture decomposed enters the decolorization tower 2, and the gas enters the condenser 5 for decolorization upwards to condense to obtain liquid methyl oleate Stored in the storage tank 16, the unvaporized liquid flows to the heater 3 at the bottom of the decolorization tower 2 and decomposes again, and the decomposed gas enters the condenser 5 to cool down after decolorization, and the product enters the storage tank 16, ...
Embodiment 2
[0030] Add 3.5 tons of acidified oil into the reaction kettle, and then add a solid acid catalyst H with an acidified oil quality of 4‰ 2 SO 4 / SiO 2 , stir and gradually raise the temperature to 90°C, and then feed methanol for esterification reaction. The time for feeding methanol is 5 hours, and the mass ratio of acidified oil to methanol is 1:1. When the acid value drops to 2.5 mg / g, the reaction ends, and then The liquid crude methyl ester is added to a rectification device for rectification and purification to obtain methyl oleate, and the yield of the prepared methyl oleate is 93.1%.
Embodiment 3
[0032] Add 3.5 tons of acidified oil into the reaction kettle, and then add a solid acid catalyst H with an acidified oil quality of 6‰ 2 SO 4 / SiO 2 , stir and gradually raise the temperature to 93°C, then feed methanol for esterification reaction, the time for feeding methanol is 4h, the mass ratio of acidified oil to methanol is 1.5:1, when the acid value drops to 2.3mg / g, the reaction ends, and then The liquid crude methyl ester is added to a rectification device for rectification and purification to obtain methyl oleate, and the yield of the prepared methyl oleate is 94%.
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