CN104973748B - A kind of electro-osmosis sludge dewatering composite filter band - Google Patents
A kind of electro-osmosis sludge dewatering composite filter band Download PDFInfo
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Abstract
本发明的目的是提供一种电渗透污泥脱水复合滤带。本发明的技术方案为:包括复合滤带和若干个绝缘护套,复合滤带由第一聚酯层、粗颗粒吸附层、若干个导电带、第二聚酯层、细颗粒吸附层和吸水层组成。该复合滤带分为双层过滤程序,污泥中的大颗粒物会被粗颗粒吸附层所吸附;那些细微颗粒物会被细颗粒吸附层所吸附;该复合滤带下部的吸水层是由两个边缘吸水层和整体吸水层组成,并且在整个复合滤带裸露的两边加设绝缘护套,对工作人员起到了一定的保护效果。该复合滤带采用多层交叉复合编织而成,并且具有耐酸、耐碱、耐磨损、耐高温的作用,使用寿命长,滤布稳定性高,透水性能好,便于平展,不会出现打折撕裂现象,安全系数高。
The object of the present invention is to provide a composite filter belt for electroosmotic sludge dewatering. The technical scheme of the present invention is: comprising a composite filter belt and several insulating sheaths, the composite filter belt is composed of a first polyester layer, a coarse particle adsorption layer, several conductive tapes, a second polyester layer, a fine particle adsorption layer and a water-absorbing layer. layer composition. The composite filter belt is divided into a double-layer filtration process. The large particles in the sludge will be adsorbed by the coarse particle adsorption layer; those fine particles will be adsorbed by the fine particle adsorption layer; The edge water-absorbing layer and the overall water-absorbing layer are composed, and insulating sheaths are added to the exposed two sides of the entire composite filter belt, which has a certain protective effect on the staff. The composite filter belt is made of multi-layer cross composite weaving, and has the functions of acid resistance, alkali resistance, wear resistance and high temperature resistance, long service life, high stability of filter cloth, good water permeability, easy to flatten, and no discount Tear phenomenon, high safety factor.
Description
技术领域technical field
本发明涉及环保技术领域,尤其涉及一种电渗透污泥脱水复合滤带。The invention relates to the technical field of environmental protection, in particular to an electroosmotic sludge dewatering composite filter belt.
背景技术Background technique
现今环保领域中,脱水滤带是污水处理、电厂脱硫、造纸洗压浆、化工、尾矿处理、钛白粉、洗选煤、植物油过滤等行业所用的重要部件。以往对于各种污泥脱水领域中,采用电渗透脱水系统的复合滤带的组成方式都比较传统,结构也比较简单;对于过滤中的细节把握不是特别理想,脱水后的效果不佳,水源浑浊;甚至有的复合滤带还缺乏安全性,工作时对于无防备的工作人员会产生安全隐患。In today's environmental protection field, the dehydration filter belt is an important component used in sewage treatment, power plant desulfurization, paper washing and pulping, chemical industry, tailings treatment, titanium dioxide, coal washing, vegetable oil filtration and other industries. In the past, for various sludge dewatering fields, the composition of the composite filter belt using the electroosmotic dewatering system is relatively traditional, and the structure is relatively simple; the details in the filtration are not particularly ideal, the effect after dehydration is not good, and the water source is turbid ; Even some composite filter belts also lack safety, which will cause potential safety hazards for unprepared staff during work.
该复合滤带分为双层过滤程序,污泥中的大颗粒物会被第一聚酯层下面的粗颗粒吸附层所吸附,此次为第一次过滤程序;然后一些微细颗粒物会落到第二聚酯层表面,该层采用十字交叉式编织方式,这种形式可以使污泥在脱水过程中对那些通过粗颗粒吸附层渗透进来的细微颗粒进行阵列分布,然后再进行第二次过滤程序,那些细微颗粒物会被第二聚酯层下面的细颗粒吸附层所吸附;第二聚酯层区分于第一聚酯层的编织方式,其目的是,在污泥进行脱水渗透过程中,不同形式的聚酯层能够驱使杂质、颗粒或者其他细微颗粒进行均匀筛选和分布,从而在脱水渗透的同时,达到逐层吸附的作用。The composite filter belt is divided into two-layer filtration procedures. The large particles in the sludge will be adsorbed by the coarse particle adsorption layer under the first polyester layer. This is the first filtration procedure; then some fine particles will fall to the second layer. On the surface of the two-polyester layer, the layer adopts a criss-cross pattern, which allows the sludge to distribute the fine particles infiltrated through the coarse particle adsorption layer in an array during the dehydration process, and then carry out the second filtration process. , those fine particles will be adsorbed by the fine particle adsorption layer under the second polyester layer; the second polyester layer is different from the weaving method of the first polyester layer. The polyester layer in the form can drive impurities, particles or other fine particles to be evenly screened and distributed, so as to achieve layer-by-layer adsorption while dehydrating and penetrating.
该复合滤带下部的吸水层,由两个边缘吸水层和整体吸水层组成,该两个边缘吸水层平行位于复合滤带的两侧,主要是在脱水的过程中对复合滤带中各个层次边缘进行水分的吸收。整体吸水层主要是在脱水的过程中对复合滤带进行水分的吸收。并且在整个复合滤带裸露的两边加设绝缘护套,对工作人员起到了一定的保护效果。该复合滤带采用多层交叉复合编织而成,加设双层吸附层,使得微颗粒吸附强度极高,并且具有耐酸、耐碱、耐磨损、耐高温的作用,使用寿命长,滤布稳定性高,透水性能好,便于平展,长期使用不会出现打折撕裂现象,安全系数高。The water-absorbing layer at the bottom of the composite filter belt is composed of two edge water-absorbing layers and an overall water-absorbing layer. The two edge water-absorbing layers are located on both sides of the composite filter belt in parallel. The edges absorb moisture. The overall water-absorbing layer mainly absorbs moisture to the composite filter belt during the dehydration process. In addition, insulating sheaths are added to the exposed two sides of the entire composite filter belt, which has a certain protective effect on the staff. The composite filter belt is made of multi-layer cross composite weaving, and a double-layer adsorption layer is added, which makes the adsorption strength of micro particles extremely high, and has the functions of acid resistance, alkali resistance, wear resistance and high temperature resistance, and has a long service life. High stability, good water permeability, easy to flatten, long-term use will not appear discounted tearing phenomenon, high safety factor.
发明内容Contents of the invention
本发明的目的是提供一种耐酸、耐碱、耐磨损、耐高温、使用寿命长、水透性好的电渗透污泥脱水复合滤带。The object of the present invention is to provide an electroosmotic sludge dehydration composite filter belt with acid resistance, alkali resistance, wear resistance, high temperature resistance, long service life and good water permeability.
本发明的技术方案为:一种电渗透污泥脱水复合滤带,其特征在于:包括复合滤带和若干个绝缘护套,所述复合滤带由第一聚酯层、粗颗粒吸附层、若干个导电带、第二聚酯层、细颗粒吸附层和吸水层组成,所述第一聚酯层位于复合滤带的最上层,所述粗颗粒吸附层位于第一聚酯层的下部,所述粗颗粒吸附层与第一聚酯层为固定连接,任意所述导电带位于粗颗粒吸附层的下部,所述导电带与粗颗粒吸附层为固定连接,所述第二聚酯层位于导电带的下部,所述第二聚酯层与导电带为固定连接,所述细颗粒吸附层位于第二聚酯层的下部,所述细颗粒吸附层与第二聚酯层为固定连接,所述吸水层位于细颗粒吸附层的下部,所述吸水层由若干个边缘吸水层和整体吸水层组成,任意所述边缘吸水层位于复合滤带的一侧,所述边缘吸水层与复合滤带为固定连接,所述整体吸水层位于细颗粒吸附层的下部,所述整体吸水层与细颗粒吸附层为固定连接,任意所述绝缘护套位于边缘吸水层的一侧,所述绝缘护套与复合滤带为固定连接。The technical solution of the present invention is: a composite filter belt for electroosmotic sludge dewatering, characterized in that it includes a composite filter belt and several insulating sheaths, and the composite filter belt is composed of a first polyester layer, a coarse particle adsorption layer, It consists of several conductive belts, a second polyester layer, a fine particle adsorption layer and a water absorption layer, the first polyester layer is located at the top of the composite filter belt, and the coarse particle adsorption layer is located at the bottom of the first polyester layer, The coarse particle adsorption layer is fixedly connected to the first polyester layer, any of the conductive bands is located at the bottom of the coarse particle adsorption layer, the conductive band is fixedly connected to the coarse particle adsorption layer, and the second polyester layer is located at the bottom of the coarse particle adsorption layer. The lower part of the conductive tape, the second polyester layer is fixedly connected to the conductive tape, the fine particle adsorption layer is located at the bottom of the second polyester layer, and the fine particle adsorption layer is fixedly connected to the second polyester layer, Described water-absorbing layer is positioned at the bottom of fine particle adsorption layer, and described water-absorbing layer is made up of several edge water-absorbing layers and integral water-absorbing layer, and any described edge water-absorbing layer is positioned at the side of composite filter belt, and described edge water-absorbing layer and composite filter The belt is fixedly connected, and the integral water-absorbing layer is located at the lower part of the fine-particle adsorbing layer. The integral water-absorbing layer and the fine-particle adsorbing layer are fixedly connected. Any of the insulating sheaths is located on one side of the edge water-absorbing layer. The sleeve and the composite filter belt are fixedly connected.
进一步,所述第一聚酯层为聚酯网状结构,并且采用X形交叉式编织方式,这种形式可以使污泥在脱水前按照不规则的形式均匀分布在滤带表面。Furthermore, the first polyester layer is a polyester mesh structure, and adopts an X-shaped cross weaving method, which can make the sludge uniformly distributed on the surface of the filter belt in an irregular form before dewatering.
进一步,所述粗颗粒吸附层为尼龙吸附网或者纤维吸附网。Further, the coarse particle adsorption layer is a nylon adsorption net or a fiber adsorption net.
进一步,所述若干个导电带的个数为2个,其材质为金属,并且该2个导电带平行位于粗颗粒吸附层下部的两侧。Further, the number of the several conductive strips is 2, and the material is metal, and the 2 conductive strips are located in parallel on both sides of the lower part of the coarse particle adsorption layer.
进一步,所述第二聚酯层为聚酯网状结构,并且采用十字交叉式编织方式,这种形式可以使污泥在脱水过程中对那些通过粗颗粒吸附层渗透进来的细微颗粒进行阵列分布。Further, the second polyester layer is a polyester mesh structure, and adopts a criss-cross pattern, which can make the sludge distribute in arrays to the fine particles infiltrated through the coarse particle adsorption layer during the dehydration process. .
再进一步,该层区分于第一聚酯层的编织方式,其目的是,在污泥进行脱水渗透过程中,不同形式的聚酯层能够驱使杂质、颗粒或者其他细微颗粒进行均匀筛选和分布,从而在脱水渗透的同时,达到逐层吸附的作用。Further, this layer is different from the weaving method of the first polyester layer. The purpose is that during the sludge dehydration and infiltration process, different forms of polyester layers can drive impurities, particles or other fine particles to be evenly screened and distributed. Thus, while dehydrating and penetrating, the effect of layer-by-layer adsorption is achieved.
进一步,所述细颗粒吸附层为棉质吸附网或者纤维吸附网。Further, the fine particle adsorption layer is a cotton adsorption net or a fiber adsorption net.
进一步,所述若干个边缘吸水层的个数为2个,其材质为吸水海绵或者吸水棉布或者吸水纤维;该2个边缘吸水层平行位于复合滤带1的两侧,主要是在脱水的过程中对复合滤带1中各个层次边缘进行水分的吸收。Further, the number of the several edge water-absorbing layers is 2, and its material is water-absorbing sponge or water-absorbing cotton cloth or water-absorbing fiber; the two edge water-absorbing layers are located in parallel on both sides of the composite filter belt 1, mainly during the dehydration process In the middle, the moisture is absorbed on the edge of each layer in the composite filter belt 1.
进一步,所述整体吸水层的材质为吸水海绵或者吸水棉布或者吸水纤维,主要是在脱水的过程中对复合滤带进行水分的吸收。Further, the material of the overall water-absorbing layer is water-absorbing sponge, water-absorbing cotton cloth or water-absorbing fiber, which mainly absorbs water in the composite filter belt during the dehydration process.
进一步,所述若干个绝缘护套的个数为2个,其材质为胶质护套,该每个绝缘护套包裹于复合滤带带有边缘吸水层的一侧,其横截面积呈凹字形。Further, the number of the plurality of insulating sheaths is 2, and its material is a colloidal sheath, and each insulating sheath is wrapped on the side of the composite filter belt with an edge water-absorbing layer, and its cross-sectional area is concave. glyph.
本发明的有益效果在于:该复合滤带的第一聚酯层2采用聚酯网状结构,并且呈X形交叉式编织方式,这种形式可以使污泥在脱水前按照不规则的形式均匀分布在滤带表面。The beneficial effect of the present invention is that: the first polyester layer 2 of the composite filter belt adopts a polyester mesh structure and is in an X-shaped cross weaving manner, which can make the sludge uniform in an irregular form before dehydration distributed on the surface of the filter belt.
在脱水的过程中,该复合滤带分为双层过滤程序,污泥中的大颗粒物会被第一聚酯层下面的粗颗粒吸附层所吸附,此次为第一次过滤程序;然后一些微细颗粒物会落到第二聚酯层表面,该层采用十字交叉式编织方式,这种形式可以使污泥在脱水过程中对那些通过粗颗粒吸附层渗透进来的细微颗粒进行阵列分布,然后再进行第二次过滤程序,那些细微颗粒物会被第二聚酯层下面的细颗粒吸附层所吸附;第二聚酯层区分于第一聚酯层的编织方式,其目的是,在污泥进行脱水渗透过程中,不同形式的聚酯层能够驱使杂质、颗粒或者其他细微颗粒进行均匀筛选和分布,从而在脱水渗透的同时,达到逐层吸附的作用。In the process of dehydration, the composite filter belt is divided into two-layer filtration procedures, and the large particles in the sludge will be adsorbed by the coarse particle adsorption layer under the first polyester layer. This is the first filtration procedure; then some The fine particles will fall to the surface of the second polyester layer. This layer adopts a criss-cross weave pattern. This form can make the sludge distribute in arrays to the fine particles that penetrate through the coarse particle adsorption layer during the dehydration process, and then For the second filtration process, those fine particles will be adsorbed by the fine particle adsorption layer under the second polyester layer; the second polyester layer is different from the weaving method of the first polyester layer. In the process of dehydration and infiltration, different forms of polyester layers can drive impurities, particles or other fine particles to be evenly screened and distributed, so as to achieve layer-by-layer adsorption during dehydration and infiltration.
该复合滤带下部的吸水层,由两个边缘吸水层和整体吸水层组成,该两个边缘吸水层平行位于复合滤带的两侧,主要是在脱水的过程中对复合滤带中各个层次边缘进行水分的吸收。整体吸水层主要是在脱水的过程中对复合滤带进行水分的吸收。并且在整个复合滤带裸露的两边加设绝缘护套,对工作人员起到了一定的保护效果。该复合滤带采用多层交叉复合编织而成,加设双层吸附层,使得微颗粒吸附强度极高,并且具有耐酸、耐碱、耐磨损、耐高温的作用,使用寿命长,滤布稳定性高,透水性能好,便于平展,长期使用不会出现打折撕裂现象,安全系数高。The water-absorbing layer at the bottom of the composite filter belt is composed of two edge water-absorbing layers and an overall water-absorbing layer. The two edge water-absorbing layers are located on both sides of the composite filter belt in parallel. The edges absorb moisture. The overall water-absorbing layer mainly absorbs moisture to the composite filter belt during the dehydration process. In addition, insulating sheaths are added to the exposed two sides of the entire composite filter belt, which has a certain protective effect on the staff. The composite filter belt is made of multi-layer cross composite weaving, and a double-layer adsorption layer is added, which makes the adsorption strength of micro particles extremely high, and has the functions of acid resistance, alkali resistance, wear resistance and high temperature resistance, and has a long service life. High stability, good water permeability, easy to flatten, long-term use will not appear discounted tearing phenomenon, high safety factor.
附图说明Description of drawings
图1为本发明的截面主视图。Fig. 1 is a sectional front view of the present invention.
图2为本发明的逐层拆解结构示意图。Fig. 2 is a schematic diagram of the layer-by-layer dismantling structure of the present invention.
图3为本发明的第一聚酯层局部放大示意图。Fig. 3 is a partially enlarged schematic view of the first polyester layer of the present invention.
图4为本发明的第二聚酯层局部放大示意图。Fig. 4 is a partially enlarged schematic view of the second polyester layer of the present invention.
其中: 1、复合滤带 2、第一聚酯层 3、粗颗粒吸附层Among them: 1. Composite filter belt 2. The first polyester layer 3. Coarse particle adsorption layer
4、导电带 5、第二聚酯层 6、细颗粒吸附层 4. Conductive tape 5. Second polyester layer 6. Fine particle adsorption layer
7、吸水层 8、边缘吸水层 9、整体吸水层 7. Water absorption layer 8. Edge water absorption layer 9. Overall water absorption layer
10、绝缘护套 10. Insulation sheath
具体实施方式Detailed ways
下面结合附图对本发明的具体实施方式做出简要说明。The specific implementation manners of the present invention will be briefly described below in conjunction with the accompanying drawings.
如图1、图2、图3、图4所示一种电渗透污泥脱水复合滤带,其特征在于:包括复合滤带1和若干个绝缘护套10,所述复合滤带1由第一聚酯层2、粗颗粒吸附层3、若干个导电带4、第二聚酯层5、细颗粒吸附层6和吸水层7组成,所述第一聚酯层2位于复合滤带1的最上层,所述粗颗粒吸附层3位于第一聚酯层2的下部,所述粗颗粒吸附层3与第一聚酯层2为固定连接,任意所述导电带4位于粗颗粒吸附层3的下部,所述导电带4与粗颗粒吸附层3为固定连接,所述第二聚酯层5位于导电带4的下部,所述第二聚酯层5与导电带4为固定连接,所述细颗粒吸附层6位于第二聚酯层5的下部,所述细颗粒吸附层6与第二聚酯层5为固定连接,所述吸水层7位于细颗粒吸附层6的下部,所述吸水层7由若干个边缘吸水层8和整体吸水层9组成,任意所述边缘吸水层8位于复合滤带1的一侧,所述边缘吸水层8与复合滤带1为固定连接,所述整体吸水层9位于细颗粒吸附层6的下部,所述整体吸水层9与细颗粒吸附层6为固定连接,任意所述绝缘护套10位于边缘吸水层8的一侧,所述绝缘护套10与复合滤带1为固定连接。所述第一聚酯层2为聚酯网状结构,并且采用X形交叉式编织方式,这种形式可以使污泥在脱水前按照不规则的形式均匀分布在滤带表面。所述粗颗粒吸附层3为尼龙吸附网或者纤维吸附网。所述若干个导电带4的个数为2个,其材质为金属,并且该2个导电带4平行位于粗颗粒吸附层3下部的两侧。所述第二聚酯层5为聚酯网状结构,并且采用十字交叉式编织方式,这种形式可以使污泥在脱水过程中对那些通过粗颗粒吸附层3渗透进来的细微颗粒进行阵列分布;该层区分于第一聚酯层2的编织方式,其目的是,在污泥进行脱水渗透过程中,不同形式的聚酯层能够驱使杂质、颗粒或者其他细微颗粒进行均匀筛选和分布,从而在脱水渗透的同时,达到逐层吸附的作用。所述细颗粒吸附层6为棉质吸附网或者纤维吸附网。所述若干个边缘吸水层8的个数为2个,其材质为吸水海绵或者吸水棉布或者吸水纤维;该2个边缘吸水层8平行位于复合滤带1的两侧,主要是在脱水的过程中对复合滤带1中各个层次边缘进行水分的吸收。所述整体吸水层9的材质为吸水海绵或者吸水棉布或者吸水纤维,主要是在脱水的过程中对复合滤带1进行水分的吸收。所述若干个绝缘护套10的个数为2个,其材质为胶质护套,该每个绝缘护套10包裹于复合滤带1带有边缘吸水层8的一侧,其横截面积呈凹字形。As shown in Figure 1, Figure 2, Figure 3 and Figure 4, an electro-osmotic sludge dewatering composite filter belt is characterized in that it includes a composite filter belt 1 and several insulating sheaths 10, and the composite filter belt 1 consists of a first A polyester layer 2, a coarse particle adsorption layer 3, several conductive tapes 4, a second polyester layer 5, a fine particle adsorption layer 6 and a water absorption layer 7, the first polyester layer 2 is located on the composite filter belt 1 The uppermost layer, the coarse particle adsorption layer 3 is located at the bottom of the first polyester layer 2, the coarse particle adsorption layer 3 is fixedly connected to the first polyester layer 2, and any of the conductive strips 4 is located in the coarse particle adsorption layer 3 The lower part of the conductive belt 4 is fixedly connected to the coarse particle adsorption layer 3, the second polyester layer 5 is located at the bottom of the conductive belt 4, and the second polyester layer 5 is fixedly connected to the conductive belt 4, so The fine particle adsorption layer 6 is located at the bottom of the second polyester layer 5, and the fine particle adsorption layer 6 is fixedly connected with the second polyester layer 5, and the water absorption layer 7 is located at the bottom of the fine particle adsorption layer 6. Water-absorbing layer 7 is made up of several edge water-absorbing layers 8 and integral water-absorbing layer 9, and any described edge water-absorbing layer 8 is positioned at the side of composite filter belt 1, and described edge water-absorbing layer 8 is fixedly connected with composite filter belt 1, and described The integral water-absorbing layer 9 is positioned at the bottom of the fine particle adsorption layer 6, and the integral water-absorbing layer 9 is fixedly connected to the fine particle adsorption layer 6, and any of the insulating sheaths 10 is positioned on one side of the edge water-absorbing layer 8, and the insulating sheath 10 is fixedly connected with composite filter belt 1. The first polyester layer 2 is a polyester mesh structure, and adopts an X-shaped cross weaving method, which allows the sludge to be evenly distributed on the surface of the filter belt in an irregular manner before dehydration. The coarse particle adsorption layer 3 is a nylon adsorption net or a fiber adsorption net. The number of the plurality of conductive strips 4 is two, and the material is metal, and the two conductive strips 4 are located in parallel on both sides of the lower part of the coarse particle adsorption layer 3 . The second polyester layer 5 is a polyester mesh structure, and adopts a criss-cross pattern, which can make the fine particles infiltrated through the coarse particle adsorption layer 3 in the sludge be distributed in an array during the dehydration process. ; This layer is different from the weaving mode of the first polyester layer 2, and its purpose is that during the dehydration and infiltration process of the sludge, the polyester layers of different forms can drive impurities, particles or other fine particles to be evenly screened and distributed, thereby At the same time of dehydration and penetration, it can achieve the effect of layer-by-layer adsorption. The fine particle adsorption layer 6 is a cotton adsorption net or a fiber adsorption net. The number of said several edge water-absorbing layers 8 is 2, and its material is water-absorbing sponge or water-absorbing cotton cloth or water-absorbing fiber; The two edge water-absorbing layers 8 are located in parallel on both sides of the composite filter belt 1, mainly in the process of dehydration In the middle, the moisture is absorbed on the edge of each layer in the composite filter belt 1. The overall water-absorbing layer 9 is made of water-absorbing sponge, water-absorbing cotton cloth or water-absorbing fiber, mainly for absorbing moisture to the composite filter belt 1 during the dehydration process. The number of the plurality of insulating sheaths 10 is 2, and its material is a colloidal sheath, and each insulating sheath 10 is wrapped on the side of the composite filter belt 1 with the edge water-absorbing layer 8, and its cross-sectional area is Concave shape.
工作方式:该复合滤带1是由第一聚酯层2、粗颗粒吸附层3、若干个导电带4、第二聚酯层5、细颗粒吸附层6和吸水层7组成的一种带有电渗透污泥脱水的多层复合滤带。首先,需要将待处理的污泥置于第一聚酯层2的上部,该层采用聚酯网状结构,并且呈X形交叉式编织方式,这种形式可以使污泥在脱水前按照不规则的形式均匀分布在滤带表面。污泥相对水来说都带有轻微的负电荷,但污泥颗粒和周围介质溶液作为一个整体是电中性的,为了平衡这些负电荷,污泥颗粒表面必会吸附介质溶液中带有相反电荷的阳离子。固体颗粒表面的负电荷与其吸附的周围介质中的反离子构成所谓的双电层。在电场作用下,污泥固体颗粒表面吸附的阳离子携带水分向阴极移动,形成电渗透现象,然后通过导电带4将污泥进行脱水处理。Working method: The composite filter belt 1 is a belt composed of the first polyester layer 2, the coarse particle adsorption layer 3, several conductive belts 4, the second polyester layer 5, the fine particle adsorption layer 6 and the water absorption layer 7 Multi-layer composite filter belt with electro-osmotic sludge dewatering. First of all, it is necessary to place the sludge to be treated on the upper part of the first polyester layer 2, which adopts a polyester mesh structure and is in an X-shaped cross weave, which allows the sludge to be dehydrated according to different Regular forms are evenly distributed on the surface of the filter belt. Compared with water, sludge has a slight negative charge, but the sludge particles and the surrounding medium solution are electrically neutral as a whole. In order to balance these negative charges, the surface of the sludge particles must absorb the opposite charge in the medium solution. Charged cations. The negative charges on the surface of solid particles and the counterions in the surrounding medium they adsorb form the so-called electric double layer. Under the action of an electric field, the cations adsorbed on the surface of the sludge solid particles carry water and move to the cathode, forming an electro-osmosis phenomenon, and then the sludge is dehydrated through the conductive belt 4 .
在脱水的过程中,污泥中的大颗粒物会被第一聚酯层2下面的粗颗粒吸附层3所吸附,此次为第一次过滤程序;然后一些微细颗粒物会落到第二聚酯层5表面,该层采用十字交叉式编织方式,这种形式可以使污泥在脱水过程中对那些通过粗颗粒吸附层3渗透进来的细微颗粒进行阵列分布,然后再进行第二次过滤程序,那些细微颗粒物会被第二聚酯层5下面的细颗粒吸附层6所吸附;第二聚酯层5区分于第一聚酯层2的编织方式,其目的是,在污泥进行脱水渗透过程中,不同形式的聚酯层能够驱使杂质、颗粒或者其他细微颗粒进行均匀筛选和分布,从而在脱水渗透的同时,达到逐层吸附的作用。During the dehydration process, the large particles in the sludge will be adsorbed by the coarse particle adsorption layer 3 under the first polyester layer 2, this time is the first filtration process; then some fine particles will fall to the second polyester layer On the surface of layer 5, this layer adopts a criss-cross weaving method, which can make the sludge distribute in arrays to the fine particles that penetrate through the coarse particle adsorption layer 3 during the dehydration process, and then perform the second filtration process, Those fine particles will be adsorbed by the fine particle adsorption layer 6 under the second polyester layer 5; Among them, different forms of polyester layers can drive impurities, particles or other fine particles to be evenly screened and distributed, so as to achieve layer-by-layer adsorption while dehydrating and penetrating.
在复合滤带1的下部还附有一个吸水层7,该层由两个边缘吸水层8和整体吸水层9组成,该两个边缘吸水层8平行位于复合滤带1的两侧,主要是在脱水的过程中对复合滤带1中各个层次边缘进行水分的吸收。整体吸水层9主要是在脱水的过程中对复合滤带1进行水分的吸收。并且在整个复合滤带1裸露的两边加设绝缘护套10,对工作人员起到了一定的保护效果。该复合滤带采用多层交叉复合编织而成,加设双层吸附层,使得微颗粒吸附强度极高,并且具有耐酸、耐碱、耐磨损、耐高温的作用,使用寿命长,滤布稳定性高,透水性能好,便于平展,长期使用不会出现打折撕裂现象,安全系数高。A water-absorbing layer 7 is also attached to the bottom of the composite filter belt 1. This layer is composed of two edge water-absorbing layers 8 and an overall water-absorbing layer 9. The two edge water-absorbing layers 8 are located on both sides of the composite filter belt 1 in parallel, mainly During the dehydration process, moisture is absorbed on the edge of each layer in the composite filter belt 1 . The integral water-absorbing layer 9 mainly absorbs moisture to the composite filter belt 1 during the dehydration process. And the insulating sheath 10 is added on the exposed both sides of the whole composite filter belt 1, which plays a certain protective effect on the staff. The composite filter belt is made of multi-layer cross composite weaving, and a double-layer adsorption layer is added, which makes the adsorption strength of micro particles extremely high, and has the functions of acid resistance, alkali resistance, wear resistance and high temperature resistance, and has a long service life. High stability, good water permeability, easy to flatten, long-term use will not appear discounted tearing phenomenon, high safety factor.
以上对本发明的一个实施例进行了详细说明,但所述内容仅为本发明的较佳实施例,不能被认为用于限定本发明的实施范围。凡依本发明申请范围所作的均等变化与改进等,均应仍归属于本发明的专利涵盖范围之内。An embodiment of the present invention has been described in detail above, but the content described is only a preferred embodiment of the present invention, and cannot be considered as limiting the implementation scope of the present invention. All equivalent changes and improvements made according to the application scope of the present invention shall still belong to the scope covered by the patent of the present invention.
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WO2001007143A1 (en) * | 1999-07-22 | 2001-02-01 | Kimberly-Clark Worldwide, Inc. | Filtration media and articles incorporating the same |
CN102614713A (en) * | 2011-01-26 | 2012-08-01 | 通用电气公司 | Multiple layer HEPA filter and method of manufacture |
CN203715471U (en) * | 2014-02-14 | 2014-07-16 | 湖北合加环境设备有限公司 | Compound filter strip for electroosmosis sludge dewatering treatment equipment |
CN204874247U (en) * | 2015-06-25 | 2015-12-16 | 天津霍普环保科技有限公司 | Compound screen of electroosmosis sludge dewatering |
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WO2001007143A1 (en) * | 1999-07-22 | 2001-02-01 | Kimberly-Clark Worldwide, Inc. | Filtration media and articles incorporating the same |
CN102614713A (en) * | 2011-01-26 | 2012-08-01 | 通用电气公司 | Multiple layer HEPA filter and method of manufacture |
CN203715471U (en) * | 2014-02-14 | 2014-07-16 | 湖北合加环境设备有限公司 | Compound filter strip for electroosmosis sludge dewatering treatment equipment |
CN204874247U (en) * | 2015-06-25 | 2015-12-16 | 天津霍普环保科技有限公司 | Compound screen of electroosmosis sludge dewatering |
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