Supported transitional metal oxide catalyst and application thereof in oil peroxidation
A technology of transition metals and catalysts, applied in the application field of preparing leather fatliquoring agents, can solve problems such as pollution, and achieve the effects of increased conversion frequency, high stability and reproducibility, and low production and use costs
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Embodiment 1
[0024] Catalyst preparation:
[0025] Catalyst support γ-Al was prepared by incipient wetness method 2 o 3 (80 ~ 100 mesh) immersed in 5% cobalt nitrate solution, at 50 ° C, continue to stir to evaporate water, in the case of no obvious residual liquid on the surface of the carrier, put the loaded catalyst precursor into a 120 ° C Dry in an oven for 24 hours, and then calcined at 450°C for 10 hours in an air atmosphere. After calcination, sieve and remove catalyst powders that are too small to obtain Co 2 o 3 The finished product of supported transition metal catalyst whose converted content reaches 3% of carrier mass.
[0026] Preparation of leather fatliquor:
[0027] 1) Partial transesterification of oil
[0028] Mixed esters are prepared by using soybean oil with an iodine value of 120 (GB / T 5532-85) as a raw material, with an alcohol-to-oil ratio of 2:1 (molar ratio), under the catalytic promotion of 0.5wt.% sodium methoxide, and reacting at 65°C for 2 hours. have t...
Embodiment 2
[0034] Example 2: Changing the active metal oxide Co in catalyst preparation 2 o 3 The content of is 10%, and all the other are with embodiment 1.
[0035] The prepared catalyst was used to prepare the leather fatliquor. The preparation conditions and catalytic oxidation operation were the same as in Example 1. After 3 hours of oxidation reaction, the peroxide value of the product was determined to be 510 mmol / kg.
Embodiment 3
[0036] Embodiment 3: Change the carrier to SBA-15 molecular sieve in the preparation of the catalyst, and the rest are the same as in Embodiment 1.
[0037] The prepared catalyst was used to prepare the leather fatliquoring agent. The preparation conditions and catalytic oxidation operation were the same as in Example 1. After 5 hours of oxidation reaction, the peroxide value of the product was determined to be 327 mmol / kg.
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