Carbon deposit cleaning agent and its application in reproduction process of deactivation catalyst thereof
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
[0029] Add a carbon deposit cleaning agent (see Table 1 for its specific composition and content) into a 1000ml flask to hydrodesulfurize a 100ml residue MoNiP / Al after an industrial operation 2 O 3The deactivated catalyst (coded as A, coke content of 11.45wt%) was treated separately, and the treated catalyst was treated with absolute ethanol for 30 minutes, and then the change in the content of amorphous and graphite-like coke was measured with a thermogravimetry. The results are shown in Table 1.
[0030]
[0031] It can be seen from Table 1 that compared with the deactivated catalyst treated with ethanol and benzene or kerosene and gasoline alone, the amount of coke deposited on the catalyst treated with the coke deposit cleaning agent solution of the present invention is significantly reduced, especially without The relative content of shaped coke deposits is significantly reduced.
[0032] It can also be seen from Table 1 that when benzene, ethanol, gasoline, and ke...
Embodiment 2
[0039] Add the coke deposit cleaning agent (see Table 3 for its specific composition and content) into a 1000ml flask to a 100ml Mo / HZSM-5 methane aromatization catalyst after industrial operation (code B, coke content of 10.84wt% ) Were treated separately, the treated catalyst was treated with absolute ethanol for 30 minutes, and then the content of amorphous and graphite-like carbon deposits was measured with a thermogravimetry. The results are shown in Table 3.
[0040]
Carbon deposit cleaning agent
deal with
Condition
Remaining product
the amount,
wt%
Thermogravimetric results: surplus
The content of residual carbon,
wt%
Amorphous
Graphite-like
-
287ml ethanol
287ml benzene
Soak for 16h, steam
Distillation 2h
10.21
86
14
350ml propylene glycol ether
150ml chlorinated ethylene
150ml isohexanol
-
6.75
76 ...
Embodiment 3
[0049] Hydrotreating 100ml of MoNiP / Al after an industrial operation 2 O 3 The deactivated catalyst (coded as C, with a carbon deposit content of 10.21wt%) is regenerated in the following way:
[0050] First put the catalyst into the regeneration unit, first use N 2 The device is replaced, the oxygen content is adjusted to 2.0v%, and the catalyst is regenerated by burning charcoal step by step. The main control conditions for each stage are: constant temperature at 120°C for 3h; constant temperature at 200°C for 2h; constant temperature at 300°C for 1.5h; constant temperature at 500°C for 3h.
[0051] The 15ml catalyst regenerated in this way was put into the micro-reactor, and the activity evaluation was carried out according to the following conditions:
[0052] Raw material oil: 950μg / g pyridine / lamp oil; volumetric space velocity: 2.0h -1 ; Temperature: 360°C: Reaction pressure: 4.0 MPa; Hydrogen flow rate: 100 ml / min. After 12 hours of stability, samples were taken for analys...
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