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Water treating method and arrangement integrating a fixed-bacteria biological treatment and flocculation-decantation

机译:结合固定细菌生物处理和絮凝倾析的水处理方法和装置

摘要

The biological and flocculation-decantation treatment of water comprises transferring biologically treated flow to a mixing area (2) and a decantation area, extracting granulated material from decantation sludges, recycling entities in the mixing area, and removing the decantation sludges separated from the granulated material. The water treatment is carried out by flocculation-decantation using ballasted flocs. A bio-cleaned flow is obtained at the end of the treatment, contains less than 2 mg/l of suspended matters. The biological and flocculation-decantation treatment of water comprises transferring biologically treated flow to a mixing area (2) and a decantation area, extracting granulated material from decantation sludges, recycling entities in the mixing area, and removing the decantation sludges separated from the granulated material. The water treatment is carried out by flocculation-decantation using ballasted flocs. A bio-cleaned flow is obtained at the end of the treatment, contains less than 2 mg/l of suspended matters. Velocity gradient of the transformation of biologically treated flow is 10-1000 s -1. An insoluble granulated material is injected into the mixing area in which the material is denser than water. The suspended matters are aggregated around the granulated material particles. The separated decantation muds of granulated material are recycled towards the mixing area. The biological treatment of water is carried out by fixed biomass comprises bacterial bed, mobile bed bio reactor, biofilters and biological discs. The biomass is fixed on a fixed support of marbles, pebbles, plates, tapes, pall ring, raschig ring, disc/drums, or in a suspension of the water treatment. The concentration of the biologically treated flow in the suspended matter (less than 3 minutes) is obtained with an exit of the biological treatment, which is lower than 1 g/l. A flocculating reactant is injected into the mixing area. Coagulant reactant is injected in an upstream of the flocculating reactant. An independent claim is included for a water treatment device.
机译:水的生物絮凝-倾析处理包括将生物处理后的水流转移到混合区(2)和倾析区,从倾析污泥中提取粒状物料,在混合区中循环利用实体,并去除从粒状物料中分离出的倾析污泥。 。使用压载絮凝物通过絮凝-析进行水处理。在处理结束时获得了生物清洁的流,其中包含的悬浮物少于2 mg / l。水的生物絮凝和倾析处理包括将生物处理后的水流转移到混合区(2)和倾析区,从倾析污泥中提取粒状物料,在混合区中循环利用实体,并去除从粒状物料中分离出的倾析污泥。 。使用压载絮凝物通过絮凝-析进行水处理。在处理结束时获得了生物清洁的流,其中包含的悬浮物少于2 mg / l。经生物处理的流转化的速度梯度为10-1000 s -1>。将不溶的颗粒状物料注入混合区,在该区域中物料比水浓。悬浮物在粒状材料颗粒周围聚集。将分离出的倾析出的粒状物料泥浆再循环至混合区。水的生物处理是通过固定的生物质进行的,该生物质包括细菌床,移动床生物反应器,生物滤池和生物盘。生物质固定在大理石,鹅卵石,板,带,鲍尔环,拉西环,圆盘/桶的固定支撑物上,或在水处理的悬浮液中固定。经过生物处理的出口获得的悬浮液中经过生物处理的流的浓度(少于3分钟)低于1 g / l。将絮凝反应物注入混合区域。凝结剂被注入到絮凝剂的上游。水处理装置包括独立权利要求。

著录项

  • 公开/公告号ZA200803136B

    专利类型

  • 公开/公告日2009-02-25

    原文格式PDF

  • 申请/专利权人 OTV SA.;

    申请/专利号ZA20080003136

  • 申请日2008-04-09

  • 分类号B01D;C02F;

  • 国家 ZA

  • 入库时间 2022-08-21 19:25:18

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