Carbon deposit cleaning agent and its application in reproduction process of carbon deposit deactivation catalyst
A technology for deactivating catalysts and cleaning agents, which is used in catalyst regeneration/reactivation, chemical/physical process, physical/chemical process catalysts, etc., to reduce carbon deposits and reduce toxicity
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Embodiment 1
[0030] In a 1000ml flask, add different carbon deposit cleaning agents (see Table 1 for specific composition and content) to hydrodesulfurize MoNiP / Al 100ml deactivated residue after an industrial operation 2 o3 Catalyst (numbering is A, carbon deposition content is 11.45wt%) is processed respectively, and the catalyst after processing continues to process with dehydrated alcohol, measures the content change of amorphous and graphite-like shape carbon deposition with thermogravimeter then, its result sees Table 1.
[0031]
[0032] As can be seen from Table 1, compared with the deactivated catalyst that only ethanol and benzene or kerosene and gasoline are processed, with the catalyst that the carbon deposit cleaning agent solution of the present invention is processed, the amount of carbon deposits all significantly reduces, especially without The relative content of stereotyped carbon deposits has been significantly reduced.
[0033] It can also be seen from Table...
Embodiment 2
[0040] In the flask of 1000ml, add carbon deposit cleaning agent (concrete composition and content see Table 3) to the 100ml Mo / HZSM-5 methane aromatization catalyst (numbering is B, carbon deposit content is 10.84wt%) after an industrial operation After treatment, the treated catalyst was continued to be treated with absolute ethanol, and then the content change of amorphous and graphite-like carbon deposits was measured with a thermogravimeter. The results are shown in Table 3.
[0041]
Carbon cleaning agent
deal with
condition
residual product
carbon content,
wt%
Thermogravimetry Results: Occupancy
The content of residual carbon deposits,
wt%
amorphous
graphite-like
-
287ml ethanol
287ml benzene
Soak for 16h, directly
Distillation 2h
10.21
86
14
80ml ether
200ml ethanolamine
150ml Dichlor...
Embodiment 3
[0050] 100ml hydrotreating MoNiP / Al after an industrial operation 2 o 3 Deactivated catalyst (coded as C, carbon deposit content is 10.21wt%) is regenerated in the following way:
[0051] First, the catalyst is loaded into the regeneration unit, and the N 2 The device is replaced, and then the oxygen content is adjusted to 2.0v%, and the catalyst is regenerated by burning charcoal step by step. The main control conditions at each stage are: 120°C, constant temperature for 3h; 200°C constant temperature for 2h; 300°C constant temperature for 1.5h; 500°C constant temperature for 3h.
[0052] The 15ml catalyst that regenerates like this is packed in microreactor, carry out activity evaluation according to following condition:
[0053] Raw oil: 950μg / g pyridine / kerosene; volumetric space velocity: 2.0h -1 ;Temperature: 360°C: Reaction pressure: 4.0MPa; Hydrogen flow rate: 100ml / min. Samples were taken for analysis after 12 hours of stabilization. The nitrogen content in the ...
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