A kind of recovery process and device of benzene partial hydrogenation catalyst
A technology of hydrogenation catalyst and recovery device, which is applied in chemical recovery, catalyst activation/preparation, physical/chemical process catalyst, etc. It can solve the problems of secondary environmental pollution, scaling and corrosion, and high environmental pressure, and reduce flushing Use of water, prevention of poisoning, effect of reducing loss
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Embodiment 1
[0049] Process of the present invention such as figure 1 As shown, the specific steps are as follows:
[0050] a) Sedimentation separation
[0051] Send the mixture of product oil and catalyst slurry from the hydrogenation reaction unit at a temperature of 130°C and a pressure of 4.9 MPa into the settling tank 1, and separate by gravity sedimentation. The catalyst slurry with high specific gravity settles to the lower part, and the product oil with low specific gravity Separation to the upper part; the catalyst slurry is sent to the hydrogenation reaction unit of the original production process to continue to participate in the reaction, and the generated oil is depressurized by the flow-limiting orifice 4 and then sent to the flash tank 2.
[0052] Among them, the generated oil mainly contains solutions of cyclohexene, cyclohexane and benzene, as well as a small amount of dissolved gases (hydrogen, methane, nitrogen), catalyst and water; the catalyst slurry is composed of ru...
Embodiment 2
[0070] a) Sedimentation separation
[0071] Send the mixture of product oil and catalyst slurry from the hydrogenation reaction unit at a temperature of 140°C and a pressure of 5.2 MPa into the settling tank 1, and separate by gravity sedimentation. The catalyst slurry with high specific gravity settles to the lower part, and the product oil with low specific gravity Separation to the upper part, the catalyst slurry is sent to the hydrogenation reaction unit of the original production process to continue to participate in the reaction, and the generated oil is depressurized by the flow-limiting orifice 4 and then sent to the flash tank 2.
[0072] Among them, the generated oil is a solution mainly containing cyclohexene, cyclohexane and benzene, and contains a small amount of dissolved gas, catalyst and water, and the dissolved gas is a mixture of hydrogen, methane and nitrogen; the catalyst slurry is made of ruthenium series noble metal (catalyst) + Zirconia (dispersant) + Zi...
Embodiment 3
[0089] The difference between Example 3 and Example 1 is that the membrane element used in the special membrane separation is a ceramic membrane with a filtration precision of 10 nm. The final catalyst recovery was 83%.
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