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Process for the preparation of catalysts based on SIALON for sewage treatment from phenol, a catalyst prepared by this method, and the method of sewage treatment from phenols with this catalyst

机译:基于SIALON的由苯酚制备的用于污水处理的催化剂的方法,用该方法制备的催化剂以及用该催化剂由苯酚进行的污水处理的方法

摘要

1. A process for producing a catalyst for purification of phenol from waste water, comprising nitriding at a nitrogen pressure of 1.0-12.0 MPa ferroalloy previously ground to a particle size of less than 160 mm in a self-sustaining mode of combustion with the subsequent filtration doazotirovaniem surround combustion mode at a nitrogen pressure of 0.15-10.0 MPa for 0.5-1.0 hours, wherein the ferroalloy used as ferrosilicoaluminum in particulate ferroalloy is further added alumina in an amount of 5.0-30.0 wt.%, the resulting nitrided alloy p azmalyvayut, isolated fraction of granules of size 0.315-2.5 mm and prepared based catalyst sialona.2. A catalyst for purification of phenol from waste water represents sialon-based catalyst obtained by the process according to Claim. 1, the size of 0.315-2.5 mm and the granules consist of main phases β-α-sialon SiAlONi zheleza.3. A method for purifying waste water from phenol at room temperature in the presence of iron-containing catalyst, which is immersed in the waste water with simultaneous supply at a rate of 0.5-1.5 liters / minute for 5-10 min a mixture of ozone with ozone 0.01-0.02 g / L, wherein that cleaning is carried out in the presence of a catalyst based on n sialon. 2.
机译:1.一种用于生产从废水中纯化苯酚的催化剂的方法,其包括以1.0-12.0MPa的铁合金在氮压力下氮化,该铁合金预先以自持燃烧方式研磨成小于160mm的粒度,随后在0.15-10.0 MPa的氮气压力下过滤doazotirovaniem环绕燃烧模式0.5-1.0小时,其中以5.0-30.0 wt。%的量进一步添加氧化铝,用作颗粒铁合金中的硅铝铁合金,得到的氮化合金pazmalyvayut ,分离出0.315-2.5mm大小的颗粒级分,并制备了基于催化剂的唾液酸树脂。2。从废水中纯化苯酚的催化剂代表通过权利要求1的方法获得的基于赛隆的催化剂。在图1中,大小为0.315-2.5mm,颗粒由主相β-α-赛隆SiAlONi zheleza组成。3。一种在室温下在含铁催化剂存在下从苯酚中纯化废水的方法,该方法浸入废水中,同时以0.5-1.5升/分钟的速度供应5-10分钟的臭氧混合物,臭氧0.01-0.02 g / L,其中该清洗是在基于正赛隆的催化剂存在下进行的。 2。

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