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Preparation method and application of grain stillage-loaded heterogeneous catalyst

A heterogeneous catalyst and distiller's grain technology, which is applied in chemical instruments and methods, water treatment of special compounds, oxidized water/sewage treatment, etc., can solve the problems of many dross, difficult to use, difficult to use distiller's grains, etc., and achieve good economic benefits Effect

Inactive Publication Date: 2017-08-04
HUBEI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, in these treatment methods, except for being used as feed and agricultural fertilizer, most of the other methods are difficult to fundamentally solve the problem of the final destination of distiller's grains, and may produce more distiller's grains
In addition, distiller's grains have complex components, high water content, difficult to store and difficult to utilize fermentation by-products such as rice husks, so there are still certain difficulties in the utilization of distiller's grains
[0003] The traditional Fenton reaction is a homogeneous catalytic reaction, and the reaction is generally carried out in an environment with a pH of 3-5, which easily leads to Fe 3+ The loss of Fe in waste liquid 3+ The content is high, which inevitably contains a certain amount of other pollutants, which is difficult to further process and dispose of, resulting in secondary pollution
After an oxidation reaction, it is discarded in the form of filter cake and cannot be recycled, which not only wastes resources, but also increases the cost of wastewater treatment

Method used

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  • Preparation method and application of grain stillage-loaded heterogeneous catalyst
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  • Preparation method and application of grain stillage-loaded heterogeneous catalyst

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preparation example Construction

[0024] The preparation method of distiller's grains supported heterogeneous catalyst of the embodiment of the present invention, described method comprises the following steps:

[0025] (1) Soak every 10-50g of dried distiller's grains in 300-1000mL acid solution with a concentration of 1-10% for 1-8h, filter, wash until neutral, and dry; calcined to obtain silicon dioxide;

[0026] (2) immersing the silicon dioxide in a concentration of 10-50% Fe 3+ Stirring in a water bath at 60-100° C. for 1-4 h in the ion solution, separating the solid from the liquid to obtain a solid, and drying the solid to obtain the heterogeneous catalyst supported on distillers grains.

[0027] The distiller's grain raw material in the embodiment of the present invention is calcined under specific conditions to obtain amorphous silica with high purity and high specific surface area, which generally does not contain harmful heavy metal ions such as lead and arsenic.

[0028] Heterogeneous catalyst m...

Embodiment 1

[0035] After the distiller's grains were washed with water for 3 times and dried, 20 g of dried distiller's grains were taken, soaked in 500 mL of 3% dilute hydrochloric acid solution for 2 hours, filtered, washed with deionized water until neutral, and dried for 10 hours. The processed distiller's grains were placed in a muffle furnace and calcined at 400°C for 20 minutes to obtain a silica product. Then immerse the silicon dioxide product in 10% ferric nitrate solution, bathe in water at 60° C. for 1 hour, filter with suction, and dry for 12 hours to obtain distiller’s grains-loaded heterogeneous catalyst.

Embodiment 2

[0037] After the distiller's grains were washed 4 times with water and dried, 30 g of dried distiller's grains were taken, soaked in 500 mL of 5% dilute hydrochloric acid solution for 4 hours, filtered, washed with deionized water until neutral, and dried for 12 hours. The processed distiller's grains were placed in a muffle furnace and calcined at 500° C. for 40 minutes to obtain a silica product. Then immerse the silicon dioxide product in 20% ferric nitrate solution, put it in a water bath at 70°C for 2 hours, filter it with suction, and dry it for 18 hours to obtain a heterogeneous catalyst supported by distiller's grains. figure 1 It is the infrared spectrogram before and after iron loading of the distiller's grains loaded heterogeneous catalyst obtained in Example 2 of the present invention.

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Abstract

The invention mainly aims at providing a preparation method and application of a grain stillage-loaded heterogeneous catalyst. The method comprises the following steps of (1) putting 10-50g of dry grain stillage into 300-1000mL of 1-10% acid solution for soaking for 1-8h, filtering and washing until neutral, drying and burning the dried grain stillage at 400-650 DEG C to obtain silicon dioxide; and (2) soaking the silicon dioxide into 10-50% Fe<3+> ion solution, stirring in a water bath at 60-95 DEG C for 1-4h, carrying out solid-liquid separation to obtain a solid and drying the solid to obtain the grain stillage-loaded heterogeneous catalyst. The Fe<3+> ion solution is taken as an iron source, the grain stillage is effectively utilized as a base material and the heterogeneous catalyst is loaded, so that the prepared catalyst is high in catalysis efficiency, no secondary pollution is generated and the catalyst can be repeatedly used for multiple times.

Description

technical field [0001] The invention belongs to the field of catalyst preparation, in particular to a preparation method and application of distiller's grains loaded heterogeneous catalyst. Background technique [0002] my country is a big country in the production and consumption of liquor, and a huge amount of distiller's grains, a by-product of brewing raw materials, are produced during the production of liquor. Because distiller's grains contain a large amount of organic matter, such as starch, cellulose, and organic acids, discarding distiller's grains as waste not only wastes resources, but also causes serious environmental pollution pressure. At present, the main utilization methods of domestic distiller's grains include: for the reproduction of raw wine, for the production of glycerin, for the cultivation of edible fungi, for the recovery of methane through fermentation, for the production of feed protein, and so on. However, in these treatment methods, except for t...

Claims

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Application Information

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IPC IPC(8): B01J23/745C02F1/72C02F101/38
CPCB01J23/745B01J23/002C02F1/722C02F1/725C02F2101/308C02F2101/38C02F2101/40C02F2305/026
Inventor 宋功武何瑜邓淳周建刚葛伊利江媛媛
Owner HUBEI UNIV
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