Technological method and equipment for separating benzene and cyclohexane mixture
A process method and a mixture technology, which are applied in the field of separating benzene and cyclohexane mixtures, can solve the problems of poor feasibility, environmental pollution, and high difficulty in operation, and achieve the effects of reducing production investment, process energy consumption, and saving costs.
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specific Embodiment 1
[0062] Embodiments of the present invention provide a process for separating a mixture of benzene and cyclohexane, comprising:
[0063] adding extractant to the mixture of benzene and cyclohexane;
[0064] Separation obtains the mixture of hexanaphthene, benzene and extractant;
[0065] Separation of benzene and extractant mixture yields benzene.
specific Embodiment 2
[0066] Such as figure 1 As shown, the embodiment of the present invention provides a kind of process method for separating the mixture of benzene and cyclohexane, comprising:
[0067] Benzene and cyclohexane mixture separation step S101:
[0068] The benzene and cyclohexane mixture 103 enters from the middle and lower part of the extractive distillation tower 106, and the extractant feed 102 enters from the middle and upper part of the extractive distillation tower 106, and the extractant feed 102 is sulfolane;
[0069] Separation of benzene and cyclohexane is carried out inside the extractive distillation tower 106;
[0070] After the cyclohexane vapor at the top of the extractive distillation tower 106 enters the condenser 107 to condense, part of the liquid phase cyclohexane flows back into the tower, and part of the liquid phase cyclohexane is extracted as the cyclohexane product 104; the bottom of the extractive distillation tower 106 After the liquid-phase benzene and ...
specific Embodiment 3
[0086] Such as figure 2 As shown, the embodiment of the present invention provides a kind of equipment for separating benzene and hexanaphthene mixture, comprising:
[0087] Extractive distillation column 106, extraction agent recovery column 207, first reboiler 108, intermediate reboiler 210, first mixer 109, second mixer 213, cooler 211, separator 212, first condenser 107 , the second condenser 208, the second reboiler 209; wherein,
[0088] The first reboiler 108 is arranged between the bottom of the extractive distillation tower 106 and the middle part of the extractant recovery tower 207;
[0089] The first mixer 109 is connected with the middle and upper part of the extractive distillation column 106;
[0090] Intermediate reboiler 210 is connected with the middle and lower part of extractant recovery tower 207;
[0091] The second reboiler 209 is connected with the bottom of the extraction agent recovery tower 207;
[0092] Separator 212, the inlet port is connecte...
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Abstract
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