Carbon deposit cleaning agent and its application in reproduction process of deactivation catalyst
A deactivated catalyst and cleaning agent technology, applied in the direction of catalyst regeneration/reactivation, chemical/physical process, physical/chemical process catalyst, etc., to achieve the effect of low toxicity and reduce carbon deposition
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Embodiment 1
[0030]In the flask of 1000ml, add carbon deposit cleaning agent (its specific composition and content are shown in Table 1) to hydrodesulfurization MoNiP / Al of 100ml deactivated residual oil after an industrial operation 2 o 3 Catalyst (numbering is A, and coke content is 11.45wt%) is processed respectively, and the catalyst after the treatment continues to process 30min with dehydrated alcohol, then measures the content change of amorphous and graphite-like shape coke with thermogravimeter, and the result See Table 1.
[0031]
[0032] As can be seen from Table 1, compared with the deactivated catalysts that have only been processed with ethanol and benzene or kerosene and gasoline, the catalyst that adopts the carbon deposit cleaning agent solution of the present invention to process, the amount of carbon deposits all significantly reduces, especially without The relative content of fixed carbon deposits decreased significantly.
[0033] It can also be seen from ...
Embodiment 2
[0040] In the flask of 1000ml, add carbon deposit cleaning agent (its concrete component and content are shown in Table 3) to the 100ml Mo / HZSM-5 methane aromatization catalyst (numbering is B, and carbon deposit content is 10.84wt% after an industrial operation) ) were processed respectively, and the treated catalyst continued to be processed with absolute ethanol for 30 min, and then the content changes of amorphous and graphite-like carbon deposits were measured with a thermogravimeter, and the results are shown in Table 3.
[0041]
Carbon cleaning agent
deal with
condition
residual product
quantity,
wt%
Thermogravimetric Results: Accounting for Residue
Carbon content, wt%
amorphous
graphite-like
-
287ml ethanol
287ml benzene
to soak
16h,
direct
to distill
2 hours
10.21
86
14
150ml propylene glycol ...
Embodiment 3
[0050] 100ml deactivated hydrofining MoNiP / Al after an industrial operation 2 o 3 Catalyst (numbering is C, carbon deposit content is 10.21wt%) adopts the following method to regenerate:
[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...
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