Carbon deposit cleaning agent and its application in reproduction of carbon deposit deactivation catalyst
A technology for deactivating catalysts and cleaning agents, applied in catalyst regeneration/reactivation, physical/chemical process catalysts, chemical instruments and methods, etc., to achieve the effect of low toxicity and reduced carbon deposition
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Embodiment 1
[0031]In a 1000ml flask, add a carbon deposit cleaning agent (see Table 1 for specific composition and content) to hydrodesulfurize MoNiP / Al 100ml deactivated residue after an industrial operation 2 o 3 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.
[0032]
[0033] As can be seen from Table 1, compared with the deactivated catalysts that are only processed with kerosene and gasoline, the amount of carbon deposits of the catalysts processed with the carbon deposit cleaning agent of the present invention are all significantly reduced, especially the relative amount of amorphous carbon deposits. The decrease in content is very obvious.
[0034] It can also be seen from Table 1 that the higher the ethyl acetate...
Embodiment 2
[0041] 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 the treatment, the treated catalyst was continued to be treated with absolute ethanol for 30 minutes, and then the content changes of amorphous and graphite-like carbon deposits were measured with a thermogravimeter. The results are shown in Table 3.
[0042]
Carbon cleaning agent
deal with
condition
residual product
carbon content,
wt%
Thermogravimetry Results: Occupancy
The content of residual carbon deposits,
wt%
amorphous
graphite-like
-
431ml kerosene
144ml petrol
Soak for 16h, straight
Distillation 2h
10.21
86
14
15ml benzene
20ml ethanol
2...
Embodiment 3
[0051] 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:
[0052] 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.
[0053] The 15ml catalyst that regenerates like this is packed in microreactor, carry out activity evaluation according to following condition:
[0054] 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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