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Method for treating wastewater of oleaginous fruits- and grain processing, comprises purifying the wastewater by separation of solid materials and oil droplets, and then concentrating in a reverse osmosis plant
Method for treating wastewater of oleaginous fruits- and grain processing, comprises purifying the wastewater by separation of solid materials and oil droplets, and then concentrating in a reverse osmosis plant
The method comprises purifying wastewater of oleaginous fruits- and grain processing by separation of solid materials and oil droplets, and then concentrating in a reverse osmosis plant (28). The wastewater passes to two microflotation plants (18, 26) that produce gas bubbles with an average diameter of 20-70 mu m. The purified wastewater after passing to the microflotation plant has a blocking index of 5 min 1and is brought without interconnection of nanofiltration and/or an ultrafiltration and/or microflotation of the reverse osmosis plant. The method comprises purifying wastewater of oleaginous fruits- and grain processing by separation of solid materials and oil droplets, and then concentrating in a reverse osmosis plant (28). The wastewater passes to two microflotation plants (18, 26) that produce gas bubbles with an average diameter of 20-70 mu m. The purified wastewater after passing to the microflotation plant has a blocking index of 5 min 1and is brought without interconnection of nanofiltration and/or an ultrafiltration and/or microflotation of the reverse osmosis plant and further cleaning section of the reverse osmosis plant. The wastewater before passing to the microflotation plant passes to a pre-separator (14) or a tube flocculator (16). A flocculant is added to the wastewater before passing the wastewater to the microflotation plant and/or to the tube flocculator. An independent claim is included for a plant for treating wastewater of oleaginous fruits- and grain processing.
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机译:该方法包括通过分离固体材料和油滴来纯化含油水果和谷物加工的废水,然后在反渗透装置中浓缩(28)。废水进入两个微浮选厂(18、26),它们会产生平均直径为20-70微米的气泡。经过纯化的废水进入微浮选厂后,其阻塞指数为5 min 1>,并且在不进行反渗透装置的纳滤和/或超滤和/或微浮选的情况下被带入。该方法包括通过分离固体材料和油滴来纯化含油水果和谷物加工的废水,然后在反渗透装置中浓缩(28)。废水进入两个微浮选厂(18、26),它们会产生平均直径为20-70微米的气泡。纯化的废水在进入微浮选设备后,其阻塞指数为5 min 1>,并且在不进行反渗透设备的纳滤和/或超滤和/或微浮选互连以及反渗透设备的进一步清洁段的情况下被带入。废水在进入微浮选设备之前先经过预分离器(14)或管式絮凝器(16)。在将废水传递到微浮选设备和/或管式絮凝器之前,先将絮凝剂添加到废水中。一个独立的索赔包括处理含油水果和谷物加工废水的工厂。
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