首页> 外国专利> Treatment of suspended material effluent having excess hydraulic content, comprises coagulating the effluents in a coagulation zone, flocculating the effluents in a flocculation zone, and decanting the effluents in a decantation zone

Treatment of suspended material effluent having excess hydraulic content, comprises coagulating the effluents in a coagulation zone, flocculating the effluents in a flocculation zone, and decanting the effluents in a decantation zone

机译:水力含量过高的悬浮物料废水的处理包括在凝结区内凝结废水,在絮凝区内凝结废水,在析区倾析废水

摘要

The process of treating suspended material effluent having excess hydraulic content, comprises coagulating the effluents in a coagulation zone (2), flocculating the effluents in a flocculation zone (3), and decanting the effluents in a decantation zone during a part of sludge contained in the suspension material separated from the clear effluent. Decantation additive having granular material such as sand is introduced into a capture zone (4), which is situated between flocculation and decantation zones. The capture zone comprises an air bubbling device in its upper part. The process of treating suspended material effluent having excess hydraulic content, comprises coagulating the effluents in a coagulation zone (2), flocculating the effluents in a flocculation zone (3), and decanting the effluents in a decantation zone during a part of sludge contained in the suspension material separated from the clear effluent. Decantation additive having granular material such as sand is introduced into a capture zone (4), which is situated between flocculation and decantation zones. The capture zone comprises an air bubbling device in its upper part for creating an air mattress (16) to ensure a homogeneous distribution of decantation additive. A quantity of air injected in the capture zone to form the air mattress is 10-15 Nm3/h by meter square. The sludge and the decantation additive are extracted from decantation zone in which the additive is separated from the sludge and reintroduced into the capture zone. The decantation additive is separated, washed and dried from the sludge using a sand separator (9) and then reintroduced into the capture zone in a form of pulverulent. An independent claim is included for an installation for treating a suspended material effluent having excess hydraulic content.
机译:处理水力含量过高的悬浮物料废水的过程包括:在凝结区(2)中凝结废水,在絮凝区(3)中凝结废水,并在其中包含的一部分污泥中在倾析区中倾析废水。悬浮物与澄清废水分离。将具有粒状材料(例如沙子)的倾析添加剂引入捕获区(4),该捕获区位于絮凝区和倾析区之间。捕获区在其上部包括鼓泡装置。处理水力含量过高的悬浮物料废水的过程包括:在凝结区(2)中凝结废水,在絮凝区(3)中凝结废水,并在其中包含的一部分污泥中在倾析区中倾析废水。悬浮物与澄清废水分离。将具有粒状材料(例如沙子)的倾析添加剂引入捕获区(4),该捕获区位于絮凝区和倾析区之间。捕获区在其上部包括一个鼓泡装置,用于产生一个气垫(16),以确保倾析添加剂的均匀分布。注入捕获区以形成气垫的空气量为10-15 Nm3> / h(平方米)。从倾析区提取污泥和倾析添加剂,在倾析区中将添加剂与污泥分离,然后重新引入捕集区。使用砂分离器(9)将倾析添加剂从污泥中分离,洗涤和干燥,然后以粉状形式重新引入捕集区。包括用于处理具有过多水力含量的悬浮物料流出物的设备的独立权利要求。

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