Method for producing 4-cumylphenol and 2.4-dicumylphenol by using phenolic tar
A technology of dicumyl phenol and cumyl phenol, which is applied in the field of producing 4-cumyl phenol and 2.4-dicumyl phenol, can solve the problems of high energy consumption, low product value, waste, etc., and achieve high yield and saving Raw materials, the effect of increasing energy consumption
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Embodiment 1
[0021] A method for producing 4-cumylphenol and 2.4-dicumylphenol from phenol tar. The method has six steps. In the first step, the phenol tar is rectified by a high-vacuum molecular distillation device, and in the second step, 1.3 tons of molecular distillation products are distilled. Add 200Kg of fresh phenol to carry out depolymerization reaction through a solid strong acid molecular sieve fixed bed reactor. In the third step, the reaction product is crystallized with a mixture of dichloroethane and toluene as a solvent. In the fourth step, the dried material is mixed with methanol, ethanol, iso Propanol mixture is solvent to carry out recrystallization, the 4-cumylphenol that is all dissolved in methanol, ethanol, isopropanol crystallization mother liquor is carried out crystallization with dichloroethane and toluene mixture as solvent, the 6th step will The results of the third and fifth steps are used for distillation of the mother liquor of the crystallized dichloroethan...
Embodiment 2
[0023] The method for producing 4-cumylphenol and 2.4-dicumylphenol with phenol tar described in embodiment 1, the operating conditions and composition of described phenol tar through high vacuum molecular distillation device rectification are as follows; high vacuum molecular distillation operation The condition is 320pa (absolute pressure), the temperature is 193oC, and the yield of the tower top material is 95-96%; the composition is cumene content 0.1%, phenol content 12.8%, α-methylstyrene content 2.8%, acetophenone content of 3.5%, dimethyl benzyl alcohol content of 0.6%, α-methylstyrene dimer content of 30.5%, p-cumylphenol content of 37.5%, 2.4-dicumylphenol content of 12.1%, and heavy component content of 0.1%.
Embodiment 3
[0025] The method for producing 4-cumylphenol and 2.4-dicumylphenol with phenol tar described in embodiment 1 or 2, the described molecular distillation product 1.3 tons is added 200Kg fresh phenol and is decomposed by solid strong acid molecular sieve fixed-bed reactor Polymerization, the operating conditions are gauge pressure 0.12Mpa, temperature 120oC, depolymerization 1.5h, phenol in the molecular distillation product and fresh phenol react with α-methylstyrene in the molecular distillation product under the action of an acidic catalyst, and simultaneously The α-methylstyrene dimer is depolymerized, and the reaction generates p-cumylphenol; then the reactor is cooled down to 100 degrees Celsius, and the α-methylstyrene monomer of 500Kg is slowly added, at a gauge pressure of 0.12Mpa and a temperature of Reaction at 100oC for 3.5h, the product obtained is as follows; the composition is cumene content 0.1%, phenol content 0.8%, α-methylstyrene content 3.8%, acetophenone cont...
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