Separation method of m-ethylphenol and paraethyl phenol
A technology of ethyl phenol and tert-butyl phenol, applied in the separation field of m-ethyl phenol and p-ethyl phenol, can solve the problems of low yield, high separation operation requirements, difficult catalyst separation and the like
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Embodiment 1
[0020] Dissolve 200 kg of a mixture of m-ethylphenol and p-ethylphenol (the mass content of m-ethylphenol is 61%, and the mass content of p-ethylphenol is 39%) in 800 kg of nitrogen methylpyrrolidone bisulfate and sulfamic acid The composite ionic liquid formed, and then the mixed solution was added into a bubble bed reactor with a constant temperature circulating water bath jacket. Turn on the circulating water bath, and control the temperature of the water bath to 50°C, then blow in isobutylene under normal pressure, and control the reaction temperature not to exceed 60°C. The ionic liquid is precipitated from it and floats on the surface of the ionic liquid. The tert-butylphenol product in the upper layer was removed and rectified under reduced pressure to obtain 172 kg of 6-tert-butyl m-ethylphenol product and 112 kg of 2-tert-butyl-p-ethylphenol product.
[0021] Add 172 kg of 6-tert-butyl-m-ethylphenol product obtained by rectification into the cracking kettle, and add ...
Embodiment 2
[0023] Dissolve 100 kg of a mixture of m-ethylphenol and p-ethylphenol (the mass content of m-ethylphenol is 36%, and the mass content of p-ethylphenol is 64%) in 900 kg of nitrogen methylpyrrolidone bisulfate and sulfamic acid The composite ionic liquid formed, and then the mixed solution was added into a bubble bed reactor with a constant temperature circulating water bath jacket. Turn on the circulating water bath, and control the temperature of the water bath to 40°C, then blow in isobutylene under the pressure of 0.2MPa, and control the reaction temperature not to exceed 50°C. It is precipitated from the ionic liquid and floats on the surface of the ionic liquid. The tert-butylphenol product in the upper layer was removed and rectified under reduced pressure to obtain 52 kg of 6-tert-butyl-m-ethylphenol product and 93 kg of 2-tert-butyl-p-ethylphenol product.
[0024] Add 52 kg of 6-tert-butyl-m-ethylphenol product obtained by rectification into the cracking kettle, and ...
Embodiment 3
[0026] Dissolve 300 kg of a mixture of m-ethylphenol and p-ethylphenol (the mass content of m-ethylphenol is 47%, and the mass content of p-ethylphenol is 53%) in 700 kg of nitrogen methylpyrrolidone bisulfate and sulfamic acid The composite ionic liquid formed, and then the mixed solution was added into a bubble bed reactor with a constant temperature circulating water bath jacket. Turn on the circulating water bath, and control the temperature of the water bath to 60°C, then blow in isobutylene under the pressure of 0.5MPa, and control the reaction temperature not to exceed 70°C. It is precipitated from the ionic liquid and floats on the surface of the ionic liquid. The tert-butylphenol product in the upper layer was removed and rectified under reduced pressure to obtain 201 kg of 6-tert-butyl m-ethylphenol product and 229 kg of 2-tert-butyl-p-ethylphenol product.
[0027] Add 201 kg of 6-tert-butyl m-ethylphenol product obtained from rectification into the cracking kettle,...
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