首页> 外国专利> Method for photocatalytic treatment of wastewater containing oxidizing component with iron ions, comprises supplying a compound containing oxidation agent and iron(II)ions to wastewater and adjusting the pH-value of the mixture

Method for photocatalytic treatment of wastewater containing oxidizing component with iron ions, comprises supplying a compound containing oxidation agent and iron(II)ions to wastewater and adjusting the pH-value of the mixture

机译:用铁离子光催化处理含氧化成分的废水的方法,包括向废水中加入含氧化剂和铁(II)离子的化合物并调节混合物的pH值

摘要

The method for photocatalytic treatment of wastewater containing oxidizing component in a pH value of 2.5-4 with iron ions, comprises supplying a compound containing oxidation agent and iron(II)ions to waste water, adjusting the pH-value of the mixture in 2.8-3.5, irradiating the mixture with sunlight in UV- and/or visible region of the spectrum, adjusting the pH-value of the mixture 6.5-7.5, separating the formed solid iron hydroxide from the mixture by solid-fluid separation, and dissolving the solid iron hydroxide in a solution with a pH-value of = 2. The method for photocatalytic treatment of wastewater containing oxidizing component in a pH value of 2.5-4 with iron ions, comprises supplying a compound containing oxidation agent and iron(II)ions to waste water, adjusting the pH-value of the mixture in 2.8-3.5, irradiating the mixture with sunlight in UV- and/or visible region of the spectrum, adjusting the pH-value of the mixture to 6.5-7.5, separating the formed solid iron hydroxide from the mixture by solid-fluid separation, and dissolving the solid iron hydroxide in a solution with a pH-value of = 2. The iron ions are precipitated in a pH-value of 6.5-7.5 and fluid and solid and solvent of retained iron hydroxide are separated in a pH-value of = 3, where the solid dissolved in the acid solution leads for the treatment of wastewater according to photo-Fenton principle. The iron(II)ions are used in an initial concentration of 5-50 mg/l as iron ion source. The oxidation agent is hydrogen peroxide. The pH-value is adjusted with sulfuric acid and/or sodium hydroxide solution. The treatment of the mixture with visible or UV-light is carried out in a wavelength range of 200-600 nm. The solid is separated by a microfilter in a separation limit of 0.2 mu m and through the use of candle filters. The separated solid dissolves in a pH-value of = 2.0 through backwashing the microfilters. The compound containing the iron(II)ions and the oxidation agent is supplied to the wastewater. The oxidation agent and the recycled iron solution are mixed together and supplied to the wastewater or the recycled iron solution is mixed with a complexing agent and the mixture is supplied to the wastewater.
机译:用铁离子光催化处理pH值为2.5-4的含氧化成分的废水的方法,该方法包括向废水中提供含氧化剂和铁(II)离子的化合物,将混合物的pH值调整为2.8- 3.5,在光谱的紫外和/或可见光区域用阳光照射混合物,将混合物的pH值调节为6.5-7.5,通过固液分离从混合物中分离出生成的固体氢氧化铁,并溶解固体pH值= 2的溶液中的氢氧化铁。用铁离子光催化处理pH值为2.5-4的含氧化成分的废水的方法,包括将含氧化剂和铁(II)离子的化合物提供给废水,将混合物的pH值调节到2.8-3.5,在光谱的UV和/或可见光区域用阳光照射混合物,将混合物的pH值调节到6.5-7.5,分离形成的固体铁氢氧化物通过固-液分离从混合物中分离出de,并将固体氢氧化铁溶解在pH值为= 2的溶液中。铁离子在pH值为6.5-7.5时沉淀出来,并保留了液体,固体和溶剂氢氧化铁的pH值= 3,其中溶解在酸性溶液中的固体根据光芬顿原理用于废水处理。铁离子的初始浓度为5-50 mg / l。氧化剂是过氧化氢。用硫酸和/或氢氧化钠溶液调节pH值。用可见光或紫外光处理混合物是在200-600 nm的波长范围内进行的。固体通过微滤器以0.2微米的分离极限进行分离,并通过使用烛式过滤器进行分离。通过反洗微滤器,分离出的固体溶解在pH值= 2.0中。含有铁离子和氧化剂的化合物被供应到废水中。将氧化剂和循环铁溶液混合在一起并提供给废水,或者将循环铁溶液与络合剂混合,然后将混合物提供给废水。

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