Elaboration of an advanced ceramic made of recycled industrial steel waste
US-11787745-B2 · Oct 17, 2023 · US
US2025305074A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025305074-A1 |
| Application number | US-202418678935-A |
| Country | US |
| Kind code | A1 |
| Filing date | May 30, 2024 |
| Priority date | Mar 28, 2024 |
| Publication date | Oct 2, 2025 |
| Grant date | — |
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A method for stabilizing a reducing slag includes the steps of: subjecting a reducing slag which contains an alkaline earth metal oxide to a drying treatment, so as to obtain a dried reducing slag; mixing a urease-producing bacterium, a fermentation medium, and a nutrient, followed by conducting a fermentation treatment, so as to obtain a fermentation product containing urease; subjecting the fermentation product to a foam fractionation treatment, so as to obtain a foam containing urease; mixing the dried reducing slag, the foam containing urease, and urea, followed by conducting a urea hydrolysis reaction and a precipitation reaction in sequence, so as to obtain a product containing a stabilized reducing slag and a residual liquid; and subjecting the product to a solid-liquid separation treatment, so as to separate the stabilized reducing slag and the residual liquid from the product.
Opening claim text (preview).
What is claimed is: 1 . A method for stabilizing a reducing slag, comprising the steps of: (a) subjecting a reducing slag which contains an alkaline earth metal oxide to a drying treatment, so as to obtain a dried reducing slag, the alkaline earth metal oxide being selected from the group consisting of calcium oxide, magnesium oxide, and a combination thereof; (b) mixing a urease-producing bacterium, a fermentation medium, and a nutrient, followed by conducting a fermentation treatment, so as to obtain a fermentation product containing urease; (c) subjecting the fermentation product containing urease obtained in step (b) to a foam fractionation treatment, so as to obtain a foam containing urease, a concentration of the urease in the foam being greater than a concentration of the urease in the fermentation product; (d) mixing the dried reducing slag obtained in step (a), the foam containing urease obtained in step (c), and urea, followed by conducting a urea hydrolysis reaction and a precipitation reaction in sequence, so as to obtain a product containing a stabilized reducing slag and a residual liquid; and (e) subjecting the product obtained in step (d) to a solid-liquid separation treatment, so as to separate the stabilized reducing slag and the residual liquid from the product. 2 . The method as claimed in claim 1 , wherein in step (b), the urease-producing bacterium is an aerobic bacterium selected from the group consisting of Sporosarcina pasteurii, Bacillus subtilis , and a combination thereof. 3 . The method as claimed in claim 1 , wherein in step (b), the urease-producing bacterium is an anaerobic bacterium selected from the group consisting of Lactobacillus plantarum, Lactobacillus rhamnosus, Lactobacillus fermentum , and combinations thereof. 4 . The method as claimed in claim 1 , wherein in step (c), the foam fractionation treatment is conducted by introducing a gas into the fermentation product containing urease, so as to generate the foam containing urease. 5 . The method as claimed in claim 4 , wherein the gas is air. 6 . The method as claimed in claim 1 , wherein in step (a), the reducing slag is subjected to a sterilization treatment before or simultaneously with the drying treatment, the sterilization treatment being conducted using ultraviolet light. 7 . The method as claimed in claim 1 , wherein in step (a), the dried reducing slag is further subjected to a sterilization treatment after the drying treatment, the sterilization treatment being conducted using ultraviolet light. 8 . The method as claimed in claim 1 , wherein in step (a), the drying treatment is conducted using sunlight. 9 . The method as claimed in claim 1 , wherein in step (b), the fermentation treatment is conducted at a temperature ranging from 15° C. to 40° C. for a time period ranging from 16 hours to 120 hours. 10 . The method as claimed in claim 1 , wherein in step (c), the foam fractionation treatment is conducted at a temperature ranging from 15° C. to 40° C. 11 . The method as claimed in claim 1 , wherein in step (d), the urea hydrolysis reaction and the precipitation reaction are conducted at a temperature ranging from 15° C. to 40° C.
Physical or chemical treatment of slags · CPC title
Working-up slag · CPC title
Treatment of liquid slag · CPC title
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