Method for preparing cyclohexane by hydrogenating benzene
A technology for hydrogenation of cyclohexane and benzene, which is applied in the fields of hydrogenation to hydrocarbons, organic chemistry, etc.
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Embodiment 1
[0033] 1. Preparation of cyclohexane catalyst by hydrogenation of cobalt-based benzene at low temperature
[0034] 146g Co(NO 3 ) 2 ·6H 2 O was dissolved in 60 mL deionized water and loaded onto 70 g SiO by impregnation 2 Carrier (commercially available), baked at 110°C for 12 hours, and calcined at 500°C for 6h to obtain the catalyst before reduction.
[0035] 2. Evaluation of the catalyst for the low temperature hydrogenation of cobalt-based benzene to prepare cyclohexane in the first reactor.
[0036] Put 0.2 g of the above catalyst in a fixed-bed micro-reactor, and reduce it with hydrogen-nitrogen mixed gas at 500° C. for 2 h, and the flow rates of hydrogen and nitrogen are both 30 mL / min. The cobalt metal content of the catalyst after reduction was 29.6% by weight.
[0037] Feed reaction gas into the above reactor, including hydrogen 10mL / min, nitrogen 40mL / min, benzene is injected by a micropump, flow rate 0.5mL / h, brought into the catalyst layer bed in the reaction...
Embodiment 2
[0048] The cobalt-based catalyst prepared in Example 1 and the nickel-based catalyst are loaded into the first reactor and the second reactor respectively, and the pressure of the reactor is adjusted to 0.8MPa, and the temperature of the first reactor is 50° C., and the second reactor The temperature is 140°C, and the volumetric space velocity of benzene is 4h -1 , the molar ratio of hydrogen to benzene is 15, and according to the above conditions, benzene and hydrogen are mixed and passed into gas-phase series double fixed-bed reactors for continuous hydrogenation reaction to obtain cyclohexane.
Embodiment 3
[0050] The cobalt-based catalyst prepared in Example 1 and the nickel-based catalyst are loaded into the first reactor and the second reactor respectively, and the pressure of the regulator reactor is 1MPa, the temperature of the first reactor is 100°C, and the temperature of the second reactor is The temperature is 230°C and the volumetric space velocity of benzene is 1h -1 , the empty molar ratio of hydrogen to benzene is 20, according to the above conditions, benzene and hydrogen are mixed and passed into the gas-phase series double fixed-bed reactors for continuous hydrogenation reaction to obtain cyclohexane.
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