Wet-dry process compounded technology for regenerating and recovering waste and old copper-bismuth catalyst
A copper-bismuth catalyst, composite regeneration technology, applied in catalyst regeneration/reactivation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve problems such as environmental pollution, activity reduction, difficulty, etc. , to achieve the effect of reducing production cost, high regeneration efficiency and improving recovery efficiency
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Embodiment 1
[0019] Such as figure 1 As shown, the invention discloses a dry-wet composite regeneration process for recovering waste copper-bismuth catalyst, comprising the following steps:
[0020] Step 1): Slurry delivery: unload the catalyst slurry from the production equipment into the first stirring buffer tank 1 at a flow rate of 20kg / h, and control the concentration of the slurry to 1%, and then transport the slurry to the hydrocyclone through the first delivery pump 2 In the hydrocyclone 3, the catalyst slurry in the lower layer treated by the hydrocyclone 3 is concentrated to 10% and enters the second stirring buffer tank 4, and the supernatant of the hydrocyclone 3 is transported to the water replenishment port of the scrubber 15 through a pipeline.
[0021] Step 2): Activation treatment: the catalyst slurry in the lower layer is transported to the top feed port of the activation furnace 6 through the second delivery pump 5 and atomized. The top of the activation furnace 6 is pro...
Embodiment 2
[0026] Such as figure 1 As shown, the invention discloses a dry-wet composite regeneration process for recovering waste copper-bismuth catalyst, comprising the following steps:
[0027] Step 1): Slurry delivery: Unload the catalyst slurry from the production equipment into the first stirring buffer tank 1 at a flow rate of 60kg / h, and control the concentration of the slurry to 20%, and then transport the slurry to the hydrocyclone through the first delivery pump 2 In the hydrocyclone 3, the lower catalyst slurry treated by the hydrocyclone 3 is concentrated to 40% and enters the second stirring buffer tank 4, and the supernatant of the hydrocyclone 3 is transported to the water replenishment port of the scrubber 15 through a pipeline.
[0028]Step 2): Activation treatment: The catalyst slurry in the lower layer is transported to the feed inlet at the top of the activation furnace 6 through the second delivery pump 5 and atomized. The top of the activation furnace 6 is provided...
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