A method for separating bridged tetrahydrocyclopentadiene isomerization products
A technology for hanging tetrahydrodicyclopentadiene and tetrahydrocyclopentadiene is applied in the field of separating bridge-type tetrahydrocyclopentadiene isomerization products, which can solve the problems of difficulty in separating trans-decalin and the like, and achieves the The rectification operation is easy to control, the condensation reaction is avoided, and the method is simple and easy to implement.
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Embodiment 1
[0023] A method for separating bridged tetrahydrocyclopentadiene isomerization products, which sequentially separates the reaction solvent with a boiling point lower than that of hanging tetrahydrodicyclopentadiene, light by-products and hanging tetrahydrodicyclopentadiene. Described light by-product comprises trans-decalin; Concrete steps are as follows:
[0024] (1) Adopt steam rectification to separate the reaction solvent whose boiling point is lower than hanging type tetrahydrocyclopentadiene: put the bridging tetrahydrocyclopentadiene isomerization product in a distillation tower, adopt steam rectification to separate, water The dosage is 0.1-1 times of the reaction solvent in the mixture to be separated, the number of theoretical plates is 10-30, the rectification pressure is 101KPa, the reflux ratio is 0.1:1—1:1, the temperature at the top of the tower is 68-71°C, and the temperature at the bottom of the tower is 81-85°C, the production liquid at the top of the tower i...
Embodiment 2
[0028] Preferably, a method for separating bridged tetrahydrocyclopentadiene isomerization products, sequentially separating the reaction solvent with a boiling point lower than that of hanging tetrahydrodicyclopentadiene, light by-products and hanging tetrahydrodicyclopentadiene Alkene, described light by-product comprises trans-decalin; Concrete steps are as follows:
[0029] (1) Adopt steam rectification to separate the reaction solvent whose boiling point is lower than hanging tetrahydrocyclopentadiene: put the bridged tetrahydrocyclopentadiene isomerization product in a distillation tower, adopt steam rectification to separate, water The dosage is 0.2-0.8 times of the reaction solvent in the mixture to be separated, the number of theoretical plates is 15-25, the rectification pressure is 101KPa, the reflux ratio is 0.1:1—1:1, the temperature at the top of the tower is 68-71°C, and the temperature at the bottom of the tower is 81-85°C, the production liquid at the top of the...
Embodiment 3
[0033] Take 1800 g of bridged tetrahydrodicyclopentadiene isomerization reaction product, which contains about 1200 g of reaction solvent cyclohexane and 600 g of deionized water. Atmospheric pressure steam rectification on a rectification column with a theoretical plate number of 20, the reflux ratio is controlled at 0.3:1, the temperature at the top of the tower is 68-70°C, and the temperature at the bottom of the tower is 81-83°C. After the rectification, the top production liquid is divided into water to obtain about 1180g cyclohexane, and the content of heavier components such as hanging tetrahydrodicyclopentadiene is less than 0.1% according to chromatographic analysis, while the cyclohexane in the remaining organic materials in the tower still The content is less than 0.01%.
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