Method for separating cracked carbon-5 fraction by front-end alkyne removal one-stage extraction
A technology for cracking carbon and removing alkynes, which can be used in the purification/separation of hydrocarbons, chemical instruments and methods, distillation purification/separation, etc. It can solve the problems of large solvent loss, difficult operation, and high energy consumption, and achieve easy operation and operation. The effect of simplicity and reduced construction costs
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Embodiment 1
[0047] Using the cracked C5 fraction of Yanshan Petrochemical Company as raw material, the separation method of the present invention is used to separate the cracked C5 fraction. The composition of the raw material and the composition of the incoming and outgoing materials of each operating device are listed in Table 1 below.
[0048] (1) Pretreatment unit: 31,000kg / h of cracked carbon five fractions and 1,500kg / h of carbon five alkanes mainly containing n-pentane and isopentane enter the middle part of azeotropic rectification tower 1, and azeotropic rectification tower 1 has 80 theoretical plates, the reflux ratio is 22, and the temperature at the top of the tower is 45°C. The light components containing C4, alkynes and alkanes are removed from the top of the tower, and the materials extracted from the bottom of the tower enter the dimerization reactor R-101. The dimerization reaction is carried out at 80-85°C to dimerize the cyclopentadiene into dicyclopentadiene, and then e...
Embodiment 2
[0055] Using the cracked C5 fraction of Yanshan Petrochemical Company as raw material, the separation method of the present invention is used to separate the cracked C5 fraction. The composition of the raw material and the composition of the incoming and outgoing materials of each operating device are listed in Table 2 below.
[0056] (1) Pretreatment unit: 31,000kg / h cracked C5 cut and 1,500kg / h isopentane enter the middle part of azeotropic rectification tower 1, and azeotropic rectification tower 1 has 80 theoretical plates, and the reflux ratio is 22, The temperature at the top of the tower is 45°C. The light components containing C4, alkynes and alkanes are removed from the top of the tower, and the materials extracted from the tower reactor enter the dimerization reactor R-101, and carry out the dimerization reaction at 80-85°C , to dimerize the cyclopentadiene into dicyclopentadiene, and then enter the pre-weight removal tower T-102. The pre-weight removal tower T-102 ha...
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