首页> 外国专利> Treating water filled with colloidal impurities in dissolved or suspension form using a treatment installation, comprises supplying the water in a flocculation zone, and introducing the mixture of water and flocs in a settling zone

Treating water filled with colloidal impurities in dissolved or suspension form using a treatment installation, comprises supplying the water in a flocculation zone, and introducing the mixture of water and flocs in a settling zone

机译:使用处理设备处理溶解或悬浮形式的充满胶体杂质的水,包括在絮凝区中供应水,以及将水和絮凝物的混合物引入沉降区中

摘要

The process for treating water filled with colloidal impurities in dissolved or suspension form using a treatment installation, comprises supplying the water in a flocculation zone (1), introducing the mixture of water and flocs in a settling zone (11), separating the treated water from the mixture of sludge and the ballast obtained from the settling of the flocs in an upper part of the settling zone, and extracting the mixture of sludge and the ballast in a lower part of the settling zone for transmitting the intermediate mixture towards an agitating zone using an endless screw. The process for treating water filled with colloidal impurities in dissolved or suspension form using a treatment installation, comprises supplying the water in a flocculation zone (1), introducing the mixture of water and flocs in a settling zone (11), separating the treated water from the mixture of sludge and the ballast obtained from the settling of the flocs in an upper part of the settling zone, extracting the mixture of sludge and the ballast in a lower part of the settling zone for transmitting the intermediate mixture towards an agitating zone using an endless screw, extracting the mixture of sludge and the ballast present in the agitating zone for carrying out a sludge/ballast separation by hydrocyclone, recycling the sludge underflow from hydrocyclone in the flocculation zone, extracting a part of the sludge obtained from the overflow of the hydrocyclone and recirculating the other part of the sludge in the agitating zone, storing the overflowed sludge in a cover (31), and measuring a level of the sludge and ballast present in the intermediate mixture. A ballast is constituted of an insoluble granular material heavier than the water and a reactive flocculant forming the flocs, where the material having adsorption and ion or molecule exchange properties is resin and activated carbon powder. A parameter representating a concentration of water filled with impurities is continuously measured before or during the water entering into the flocculation zone by continuously deducting a quantity of ballast for obtaining the treated water with a predetermined quality. A concentration of ballast of extracted mixture from the settling zone or the mixture present in the flocculation zone is continuously measured by continuously deducting the concentration of ballast in the installation from the extracted mixture concentration of the settling zone. The flocculation zone is refilled by ballast when the concentration of ballast present in the installation is lower than a predetermined threshold. A coagulating reagent is continuously injected in the water before its entry in the flocculation zone according to their predetermined amount, where the reagent adjusts a pH according the predetermined amount. The parameter representing the concentration of water filled with impurities is a concentration of water from matter in suspension (total MES), which is calculated using the parameters consisting of the concentration of water in suspension material and in organic material, the concentration of microorganisms and micropollutants in raw water, and predetermined amount of coagulating reagent. The treated water with predetermined quality is determined using a formula Y = aX(b)+c, where Y is ballast concentration, X is the concentration of the total MES, a is 0.5-1, b is 0.3-1 and c is 0-2. The amount of reactive flocculant distributed in the flocculation zone is continuously adjusted for obtaining the treated water with predetermined quality, where the distribution is carried out by hydraulic distribution device. An auxiliary liquid of 5-20 vol.% is injected in the hydrocyclone. A completely immersed flux guide structure and an axial turbulent flow of water to be treated are delimited within the flocculation zone by agitation. The flow coming out of the flux guide structure is converted into axial flow using a static flow distribution device. An independent claim is included for an installation for treating water filled with colloidal impurities in dissolved or suspension form.
机译:使用处理设备处理填充有溶解或悬浮形式的胶体杂质的水的方法包括:在絮凝区(1)中供应水,将水和絮凝物的混合物引入沉降区(11),分离处理过的水从沉降区上部的絮凝物沉降得到的污泥和压舱物的混合物中提取沉淀物,然后在沉降区的下部提取淤泥和压载物的混合物,以将中间混合物输送到搅拌区使用无头螺钉。使用处理设备处理填充有溶解或悬浮形式的胶体杂质的水的方法包括:在絮凝区(1)中供应水,将水和絮凝物的混合物引入沉降区(11),分离处理过的水从沉降区上部的絮凝物沉降得到的污泥和压舱物的混合物中,提取沉降区下部的污泥和压舱物的混合物,以将中间混合物传送到搅拌区。循环螺杆,提取存在于搅拌区的污泥和压载物的混合物,以便通过水力旋流器进行污泥/压载物分离,回收来自絮凝区中水力旋流器的污泥底流,提取从水力旋流器并在搅拌区循环污泥的另一部分,将溢流的污泥存储在盖子(31)中,确保中间混合物中存在的污泥和压载物水平。压载物由比水重的不溶性颗粒物质和形成絮凝物的反应性絮凝剂构成,其中具有吸附和离子或分子交换特性的物质是树脂和活性炭粉末。在水进入絮凝区之前或期间,通过连续扣除一定量的压载水以获得用于获得预定质量的处理过的水,连续地测量代表充满杂质的水的浓度的参数。通过从沉降区的提取混合物浓度中连续减去设备中的镇流剂浓度,可以连续地测量从沉降区中提取的混合物或絮凝区中存在的混合物的道ast浓度。当设施中存在的压载物浓度低于预定阈值时,用压载物填充絮凝区。在凝结剂根据其预定量进入絮凝区之前,将其连续注入水中,其中,试剂根据预定量调节pH。代表充满杂质的水的浓度的参数是悬浮物中物质的水浓度(总MES),该参数是使用以下参数来计算的:悬浮物和有机物中的水浓度,微生物和微污染物的浓度在原水中加入一定量的凝结剂。使用公式Y = aX(b)+ c确定具有预定质量的处理水,其中Y是压载物浓度,X是总MES的浓度,a是0.5-1,b是0.3-1,c是0 -2。连续调节在絮凝区中分配的反应性絮凝剂的量,以获得具有预定质量的处理水,其中通过液压分配装置进行分配。将5-20体积%的辅助液体注入旋液分离器中。通过搅拌,在絮凝区内限定了完全浸入的通量导向结构和待处理水的轴向湍流。使用静态流量分配设备将从磁通量引导结构出来的流量转换为轴向流量。对于处理溶解或悬浮形式的充满胶体杂质的水的装置,包括一个独立权利要求。

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