Hydrogenation catalyst with TiO2 as carrier of non-crystal Nib alloy
An amorphous alloy, hydrogenation catalyst technology, applied in metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, hydrogenation of aromatic hydrocarbons, etc., can solve the problem of catalyst activity and mechanical strength development, etc. to solve the problem of sulfur poisoning and achieve the effect of good sulfur resistance
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Embodiment 1
[0017] TiO at 450°C 2 Carrier pretreatment for 4 hours, weigh 5gTiO 2 , slowly add 11.1ml of 1.3MNi(NO 3 ) 2 solution, stirred for 4 hours, filtered, and the filtrate was added to 11.1ml of distilled water, and 2MKBH was added dropwise at 0°C under nitrogen protection and vigorous stirring 4 The solution is 18.55ml, drop it within 15min; when no gas is generated, filter, wash the filter cake with a large amount of distilled water until neutral, then wash with absolute ethanol, and finally store it in absolute ethanol, and dry the catalyst in the shade before use , tableting, crushing, sieving.
[0018] The reaction of the present invention adopts a benzene hydrogenation and thiophene HDS reaction device combined with pulse micro-reaction-gas chromatography. Measure 1ml of the above-mentioned dried catalyst into the reactor; pulse benzene hydrogenation reaction conditions: the carrier gas is hydrogen, the flow rate is 50ml / min, and it is reduced at 140°C for 1h under hydrog...
Embodiment 2
[0022] With the catalyst prepared in embodiment 1 and Al 2 o 3 Mechanical grinding and mixing, adding Al 2 o 3 The weight percentage composition is respectively 20%, 30%, 40% and 50%, and all the other are all the same as embodiment 1.
Embodiment 3
[0024] TiO 2 The impregnation and drying process of the powder is the same as that of the comparative example, then add 18mlH 2 O, add 2M KBH dropwise under nitrogen protection and vigorous stirring at 0°C 4 33.45ml, drop within 20 minutes. All the other processing conditions and reaction conditions are with embodiment 1. The yield and selectivity of cyclohexane and the limit sulfur resistance are shown in Table 2, and the yield and selectivity of n-butane are shown in Table 3.
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