Loaded solid phase metal catalyst for magnesium desulfurization process, and preparation method thereof
A metal catalyst and magnesium desulfurization technology, which is applied in molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of secondary pollution of catalysts, achieve high reuse rate, high efficiency, and avoid secondary pollution The effect of pollution problems
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Embodiment 1
[0032] Embodiment 1: the catalytic effect of different concentration supported solid-phase metal catalysts
[0033] Weigh Co(NO 3 ) 2 ·6H 2 O0.9688g, Fe(NO 3 ) 3 9H 2 O2.8386g, Mn(NO 3 ) 2 4H 2 O2.6779g and Ni(NO 3 ) 2 ·6H 2 0.9720g, uniformly mixed and made into an aqueous solution; and 20.002g of 4A type molecular sieve after pretreatment was weighed, mixed with the configured nitrate solution, shaken at a constant speed of 120r / min for 8 hours, and left standstill for 24 hours. After filtering and washing with deionized water several times, drying at 120° C. for 10 hours, and calcining at 500° C. for 5 hours, a supported solid-phase metal catalyst was obtained.
[0034] Take the prepared catalyst and add it to the absorption slurry of five parallel magnesium desulfurization systems, the concentration of the catalyst is 10g L -1 , 20g·L -1 , 40g·L -1 , 80g·L -1 and 160g·L -1 , to compare their catalytic effects under the same reaction conditions.
[0035] Ex...
Embodiment 2
[0036] Embodiment 2: the catalytic effect of the loaded solid-phase metal catalyst of different active ingredient ratios
[0037] case2:
[0038] Weigh Co(NO 3 ) 2 ·6H 2 O0.4745g, Fe(NO 3 ) 3 9H 2 O0.3300g, Mn(NO 3 ) 2 4H 2 O0.4084g and Ni(NO 3 ) 2 ·6H 20.2375g, uniformly mixed and made into solution; and take by weighing 20.002g of 4A type molecular sieve after the pretreatment, it is mixed with the nitrate solution that configures, shake table constant speed 120r / min vibration 6 hours, leave standstill 24 hours, After filtering and washing with deionized water several times, drying at 110° C. for 12 hours, and calcining at 400° C. for 6 hours, a supported solid-phase metal catalyst was obtained. Take 4.002g of the prepared catalyst and add it to the absorption slurry of the magnesium desulfurization system, so that the catalyst concentration is 20g L -1 , the catalytic rate increased by about 0.50 times compared with the non-catalytic condition.
[0039] case3:...
Embodiment 3
[0048] Embodiment 3: the catalytic effect of the loaded solid-phase metal catalyst of different loads
[0049] case7:
[0050] Weigh Co(NO 3 ) 2 ·6H 2 O0.1493g, Fe(NO 3 ) 3 9H 2 O0.4374g, Mn(NO 3 ) 2 4H 2 O0.4127g and Ni(NO 3 ) 2 ·6H 2 0.1497g, uniformly mixed and made into solution; and 20.002g of 4A type molecular sieves after pretreatment was weighed, mixed with the configured nitrate solution, shaken at a constant speed of 120r / min for 7 hours, and left standstill for 24 hours. After filtering, washing with deionized water several times, drying at 130°C for 12 hours, and calcining at 600°C for 4 hours, a supported solid-phase metal catalyst with a loading capacity (mass fraction of total metal ions in the catalyst) of 1% was obtained. Take 4.002g of the prepared catalyst and add it to the absorption slurry of the magnesium desulfurization system, so that the catalyst concentration is 20g L -1 , the catalytic rate increased by about 0.42 times compared with the...
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