CN111375239A - Laminated self-cleaning filtering device and cleaning filtering method for sewage treatment - Google Patents
Laminated self-cleaning filtering device and cleaning filtering method for sewage treatment Download PDFInfo
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- CN111375239A CN111375239A CN202010336126.1A CN202010336126A CN111375239A CN 111375239 A CN111375239 A CN 111375239A CN 202010336126 A CN202010336126 A CN 202010336126A CN 111375239 A CN111375239 A CN 111375239A
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- 238000001914 filtration Methods 0.000 title claims abstract description 74
- 239000010865 sewage Substances 0.000 title claims abstract description 68
- 238000004140 cleaning Methods 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 79
- 238000011001 backwashing Methods 0.000 claims abstract description 33
- 230000007797 corrosion Effects 0.000 claims abstract description 12
- 238000005260 corrosion Methods 0.000 claims abstract description 12
- 238000011010 flushing procedure Methods 0.000 claims abstract description 9
- 230000000694 effects Effects 0.000 claims abstract description 7
- 238000005406 washing Methods 0.000 claims description 23
- 238000003475 lamination Methods 0.000 claims description 16
- 239000012535 impurity Substances 0.000 claims description 15
- 230000006835 compression Effects 0.000 claims description 14
- 238000007906 compression Methods 0.000 claims description 14
- 239000007787 solid Substances 0.000 claims description 13
- 229920003023 plastic Polymers 0.000 claims description 11
- 238000004062 sedimentation Methods 0.000 claims description 10
- 230000009471 action Effects 0.000 claims description 9
- 239000004033 plastic Substances 0.000 claims description 8
- 239000012530 fluid Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 4
- 239000010802 sludge Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 210000000476 body water Anatomy 0.000 claims 1
- 230000003750 conditioning effect Effects 0.000 claims 1
- 230000003247 decreasing effect Effects 0.000 claims 1
- 230000010354 integration Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D29/68—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles
- B01D29/688—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with backwash arms, shoes or nozzles with backwash arms or shoes acting on the cake side
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/603—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by flow measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/606—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by pressure measuring
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种水处理过滤设备领域,具体为一种适用于污水处理系统深度处理、循环水处理系统及中水回用系统的固体悬浮颗粒的分离,使其可以循环使用的污水处理用叠片式自清洗过滤装置及清洗过滤方法。The invention relates to the field of water treatment and filtration equipment, in particular to a sewage treatment stack suitable for advanced treatment of sewage treatment systems, separation of solid suspended particles in circulating water treatment systems and reclaimed water reuse systems so that they can be recycled. A chip-type self-cleaning filter device and a cleaning and filtering method.
背景技术Background technique
随着社会的发展,国家对污水处理工艺及出水标准提出了更高的要求,污水处理厂及污水处理设备排放标准逐级高到一级A标,甚至地表水准V类或准IV类标准,要求出水SS≤5mg/L,传统的污水处理沉淀分离工艺出水已达不到排放标准的要求,必须进行深度处理,因此各种过滤设备被广泛应用于污水处理厂及污水处理设备提标改造及深度处理中。With the development of society, the state has put forward higher requirements for sewage treatment technology and effluent standards. The discharge standards of sewage treatment plants and sewage treatment equipment are gradually increased to the first-level A standard, and even the surface level V or quasi-IV standard. The effluent SS is required to be less than or equal to 5mg/L. The effluent of the traditional sewage treatment sedimentation separation process cannot meet the requirements of the discharge standard and must undergo advanced treatment. Therefore, various filtration equipment is widely used in sewage treatment plants and sewage treatment equipment upgrading and upgrading. In-depth processing.
目前污水或废水处理过滤常用的有石英砂过滤器,活性炭过滤器,多介质过滤器等等。这些过滤器统称为机械过滤器,主要是通过过滤拦截,吸附水中的颗粒物及金属离子,这类过滤器普遍存在体积大、结构复杂、外部管路多;容易堵塞滤料、清洗时间长、耗水量大等缺陷,使得过滤器的过滤效率极大的降低。At present, the commonly used sewage or wastewater treatment filtration are quartz sand filter, activated carbon filter, multi-media filter and so on. These filters are collectively referred to as mechanical filters, which mainly intercept and absorb particulate matter and metal ions in water through filtration. Such filters are generally large in size, complex in structure, and many external pipelines; they are easy to block the filter material, have a long cleaning time, and consume a lot of energy. Defects such as large amount of water greatly reduce the filtration efficiency of the filter.
因此,提供一种体积小,效率高,能够集成到一体化污水处理设备中,同时操作简单,能够实现全自动反清洗功能的新型污水处理过滤装置,是一个亟需解决的问题。Therefore, it is an urgent problem to provide a new type of sewage treatment filtration device that is small in size, high in efficiency, can be integrated into integrated sewage treatment equipment, and at the same time is easy to operate and can realize automatic back-cleaning function.
发明内容SUMMARY OF THE INVENTION
针对上述现有技术中存在的不足,本发明提供一种集成度高、体积小、过滤效率高、反洗耗水少,具有自动反洗功能的污水处理用叠片式自清洗过滤装置及清洗过滤方法。In view of the above-mentioned deficiencies in the prior art, the present invention provides a lamination type self-cleaning filter device for sewage treatment with high integration, small volume, high filtration efficiency, low water consumption for backwashing, and automatic backwashing function and cleaning filter method.
本发明的目的是这样实现的:The object of the present invention is achieved in this way:
一种污水处理用叠片式自清洗过滤装置,包括电动控制阀1,所述的电动控制阀1设置在过滤器壳体上方,所述的过滤器壳体内设置有叠片式滤芯12;A laminated self-cleaning filter device for sewage treatment, comprising an
所述的电动控制阀1为三位五通电动控制阀1,包括阀体13,设置在阀体上方的驱动控制器11;所述的阀体13上设置有进水口A、出水口B、排污口C、外腔接口D和内腔接口E;阀体13下发设置有与壳体连接固定的外螺纹10;所述的驱动控制器11上设置有用于显示参数和控制按钮的调节操作面板14;The
所述的过滤器壳体包括通过快开式卡箍5连接固定在一起的上壳体2和下壳体3;所述的上壳体顶部设置有与外螺纹10配合连接的内螺纹结构;上壳体两侧壳体上设置有2个带有内螺纹的固定支座9,用来固定过滤器;The filter housing includes an
所述的叠片式滤芯12包括导流件6、碟片支架7、过滤碟片4和压紧弹簧7;所述的碟片支架7通过导流件6与阀体13上的内腔接口E连接;The laminated
所述的过滤碟片4为塑料制成的圆环薄片,两面均刻有一定微米尺寸的V型放射状过滤通道,若干过滤叠片重叠在一起,安装在碟片支架7上,支架末端装有压紧弹簧8,用以压紧过滤碟片4;The
所述的阀体13、包括上壳体2和下壳体3的过滤器壳体、以及位于过滤器壳体内的导流件6、叠片支架7均由耐腐蚀高强度塑料制成;下壳体3为透明塑料材质;The
用于连接上壳体2和下壳体3的快开式卡箍5和用于压紧压紧弹簧8均为耐腐蚀不锈钢材质制作。The quick-
一种污水处理用叠片式自清洗过滤装置的清洗过滤方法,包括以下步骤:A cleaning and filtering method for a laminated self-cleaning filter device for sewage treatment, comprising the following steps:
步骤一:用于污水处理深度处理时,二沉池出水通过加压泵与过滤器进水口A连接,过滤器出水口B连接清水池或回用水系统,清洗出水由排污口C连接到排污管道,接入污泥池或回流至调节池;Step 1: When used for advanced treatment of sewage treatment, the effluent of the secondary sedimentation tank is connected to the filter inlet A through the pressurized pump, the filter outlet B is connected to the clean water tank or the reuse water system, and the cleaning effluent is connected to the sewage pipeline by the sewage outlet C. , access the sludge tank or return to the adjustment tank;
管道连接后,启动控制器进入自动控制状态,此时三位五通电动控制阀1的驱动控制器13,驱动阀芯转动至“正洗”位置,阀体进水口A和外腔接口D相通,排污口C和内腔接口E相通,出水口B处于关闭截止状态;After the pipeline is connected, the starter controller enters the automatic control state. At this time, the
此时,驱动控制器13发出指令,启动过滤加压泵,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由外腔接口D,进入叠片式滤芯12和过滤器外壳之间,在流体压力作用下,液体穿透过滤碟片,进入滤芯内部,固体杂质或悬浮物被过滤碟片拦截;At this time, the
经由滤芯过滤后的清水经由内腔接口E,从排污口流出,此时,过滤器处于“正洗”工作状态;The clean water filtered by the filter element flows out from the sewage outlet through the inner cavity interface E. At this time, the filter is in the "positive washing" working state;
在进入“正洗”工作状态时,驱动控制器13开始计时,到达设定时间后,切换至过滤状态,正洗时间一般设定为1~2分钟,正洗时间可通过调节操作面板14调整;When entering the working state of "washing", the
步骤二:到达正洗设定时间后,驱动控制器13驱动阀芯转动至“过滤”位置,阀体进水口A仍和外腔接口D相通,出水口B和内腔接口E相通,排污口C处于关闭截止状态;Step 2: After reaching the set time for positive washing, the
此时,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由外腔接口D,进入叠片式滤芯12和过滤器外壳之间,在流体压力作用下,液体穿透过滤碟片,进入滤芯内部,固体杂质或悬浮物被过滤碟片拦截;At this time, the effluent from the secondary settling tank flows in through the filter inlet A after being pressurized. Under the diversion of the
经由滤芯过滤后的清水经由内腔接口E,从出水口B流出,此时,过滤器处于“过滤”工作状态;The clean water filtered by the filter element flows out from the water outlet B through the inner cavity interface E. At this time, the filter is in the "filtering" working state;
在进入“过滤”工作状态时,驱动控制器13开始计时,随着过滤的进行,固体杂质不断被拦截、堆积,造成过滤阻力增大,差压升高,过滤效率降低,需要进入反洗状态对滤芯进行反洗;When entering the working state of "filtering", the
步骤三:在接收到反洗需求信号后,驱动控制器13驱动阀芯转动至“反洗”位置,阀体进水口A和内腔接口E相通,排污口C和外腔接口D相通,出水口B处于关闭截止状态;Step 3: After receiving the backwash demand signal, the
此时,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由内腔接口E进入滤芯内部,在流体压力作用下,压紧过滤碟片4的压紧弹簧8被压缩,重叠的碟片放松,冲洗水穿过碟片间的缝隙进入过滤器腔体,固体杂质或悬浮物经由外腔接口D从排污口排出,从而使碟片可过滤器得到反冲洗;At this time, the effluent of the secondary sedimentation tank flows into the filter inlet A after being pressurized, and enters the filter element through the inner cavity interface E under the diversion of the
由于碟片两面刻有与中心线呈一定角度的放射状V型过滤通道,在冲洗水的压力作用下,碟片产生震动与旋转,碟片上的污物被离心力甩出,水在过滤器腔体形成旋流,腔体内污物被快速清扫排出,所以本装置反冲洗极为高效快速,在几秒至几十秒内完成反冲洗过程,反洗时间可通过调节操作面板14调整;Because the two sides of the disc are engraved with radial V-shaped filter channels at a certain angle to the center line, under the pressure of the flushing water, the disc vibrates and rotates, the dirt on the disc is thrown out by centrifugal force, and the water is in the filter cavity. The body forms a swirling flow, and the dirt in the cavity is quickly cleaned and discharged, so the backwashing of the device is extremely efficient and fast, and the backwashing process is completed within a few seconds to tens of seconds, and the backwashing time can be adjusted by adjusting the
反洗到达设定时间后,又切换至正洗状态,为下一次过滤做准备,周而复始,从而实现过滤器的全自动自清洗和过滤过程。After the backwash reaches the set time, it switches to the normal washing state again to prepare for the next filtration, and repeats the cycle, so as to realize the automatic self-cleaning and filtration process of the filter.
所述的步骤一中:在“正洗”工作状态下,过滤后的清水并不直接从出水口B排出,而是从排污口流出,目的是冲洗过滤器滤芯和管路,避免管路中杂质进入清水系统,最大限度保证过滤效果;In the first step: in the "positive washing" working state, the filtered clean water is not directly discharged from the water outlet B, but flows out from the sewage outlet. Impurities enter the clean water system to maximize the filtering effect;
所述的步骤二中:进入反洗状态有三种控制方式,第一种是时间控制,到达过滤设定时间后,自动切换至反洗状态,过滤时间可通过调节操作面板14调整,控制器也可接受外部差压信号或流量信号,设定为差压控制模式或流量控制模式。In the second step: there are three control methods for entering the backwashing state. The first is time control. After reaching the filtering set time, it will automatically switch to the backwashing state. The filtering time can be adjusted by adjusting the
积极有益效果:本发明具有稳定的过滤效率,精确的过滤效果;结构集成度高,占地小;独特的控制阀结构,一阀实现过滤和反洗全自动控制;高效的自清洗性能,冲洗时节能节水;不需设置反冲洗水泵,投资少;耐腐蚀性能好,使用寿命长;对于污水处理排放标准要求日益严苛的当下,作为二级污水处理系统出水的后端深度处理装置,该发明具有广阔的应用前景。Positive and beneficial effects: the invention has stable filtration efficiency and accurate filtration effect; high structural integration and small footprint; unique control valve structure, one valve realizes automatic control of filtration and backwashing; efficient self-cleaning performance, flushing Energy saving and water saving; no need to install backwash pump, low investment; good corrosion resistance and long service life; as the requirements of sewage treatment and discharge standards are becoming more and more stringent, as a back-end advanced treatment device for the effluent of the secondary sewage treatment system, The invention has broad application prospects.
附图说明Description of drawings
图1为本发明的半剖结构示意图:Fig. 1 is the half-section structure schematic diagram of the present invention:
图2为本发明的左视结构示意图;Fig. 2 is a left-view structural schematic diagram of the present invention;
图3为本发明的轴侧图:Fig. 3 is the axonometric view of the present invention:
图4为本发明的立体图:Fig. 4 is the perspective view of the present invention:
图5为本发明的主视图:Fig. 5 is the front view of the present invention:
图中为:电动控制阀1、上壳体2、下壳体3、过滤碟片4、快开式卡箍5、导流件6、碟片支架7、压紧弹簧8、固定支座9、连接螺纹10、驱动控制器11、叠片式滤芯12、阀体13、操作控制面板14、进水口A、出水口B、排污口C、外腔接口D、内腔接口E。The picture shows:
具体实施方式Detailed ways
下面结合附图及实施例,对本发明做进一步的说明:Below in conjunction with accompanying drawing and embodiment, the present invention is further described:
如图1所示,一种污水处理用叠片式自清洗过滤装置,包括电动控制阀1,所述的电动控制阀1设置在过滤器壳体上方,所述的过滤器壳体内设置有叠片式滤芯12;As shown in FIG. 1, a laminated self-cleaning filter device for sewage treatment includes an
如图1、图5所示,所述的电动控制阀1为三位五通电动控制阀1,包括阀体13,设置在阀体上方的驱动控制器11;所述的阀体13上设置有进水口A、出水口B、排污口C、外腔接口D和内腔接口E;阀体13下发设置有与壳体连接固定的外螺纹10;所述的驱动控制器11上设置有用于显示参数和控制按钮的调节操作面板14,如图3所示;As shown in FIGS. 1 and 5 , the
所述的过滤器壳体包括通过快开式卡箍5连接固定在一起的上壳体2和下壳体3;所述的上壳体顶部设置有与外螺纹10配合连接的内螺纹结构;如图2、图4所示,上壳体两侧壳体上设置有2个带有内螺纹的固定支座9,用来固定过滤器;The filter housing includes an
所述的叠片式滤芯12包括导流件6、碟片支架7、过滤碟片4和压紧弹簧7;所述的碟片支架7通过导流件6与阀体13上的内腔接口E连接;The
所述的过滤碟片4为塑料制成的圆环薄片,两面均刻有一定微米尺寸的V型放射状过滤通道,若干过滤叠片重叠在一起,安装在碟片支架7上,支架末端装有压紧弹簧8,用以压紧过滤碟片4;The
所述的阀体13、包括上壳体2和下壳体3的过滤器壳体、以及位于过滤器壳体内的导流件6、叠片支架7均由耐腐蚀高强度塑料制成;下壳体3为透明塑料材质;The
用于连接上壳体2和下壳体3的快开式卡箍5和用于压紧压紧弹簧8均为耐腐蚀不锈钢材质制作。The quick-
实施例1Example 1
一种污水处理用叠片式自清洗过滤装置的清洗过滤方法,包括以下步骤:A cleaning and filtering method for a laminated self-cleaning filter device for sewage treatment, comprising the following steps:
步骤一:用于污水处理深度处理时,二沉池出水通过加压泵与过滤器进水口A连接,过滤器出水口B连接清水池或回用水系统,清洗出水由排污口C连接到排污管道,接入污泥池或回流至调节池;Step 1: When used for advanced treatment of sewage treatment, the effluent of the secondary sedimentation tank is connected to the filter inlet A through the pressurized pump, the filter outlet B is connected to the clean water tank or the reuse water system, and the cleaning effluent is connected to the sewage pipeline by the sewage outlet C. , access the sludge tank or return to the adjustment tank;
管道连接后,启动控制器进入自动控制状态,此时三位五通电动控制阀1的驱动控制器13,驱动阀芯转动至“正洗”位置,阀体进水口A和外腔接口D相通,排污口C和内腔接口E相通,出水口B处于关闭截止状态;After the pipeline is connected, the starter controller enters the automatic control state. At this time, the
此时,驱动控制器13发出指令,启动过滤加压泵,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由外腔接口D,进入叠片式滤芯12和过滤器外壳之间,在流体压力作用下,液体穿透过滤碟片,进入滤芯内部,固体杂质或悬浮物被过滤碟片拦截;At this time, the
经由滤芯过滤后的清水经由内腔接口E,从排污口流出,此时,过滤器处于“正洗”工作状态;The clean water filtered by the filter element flows out from the sewage outlet through the inner cavity interface E. At this time, the filter is in the "positive washing" working state;
所述的步骤一中:在“正洗”工作状态下,过滤后的清水并不直接从出水口B排出,而是从排污口流出,目的是冲洗过滤器滤芯和管路,避免管路中杂质进入清水系统,最大限度保证过滤效果;In the first step: in the "positive washing" working state, the filtered clean water is not directly discharged from the water outlet B, but flows out from the sewage outlet. Impurities enter the clean water system to maximize the filtering effect;
在进入“正洗”工作状态时,驱动控制器13开始计时,到达设定时间后,切换至过滤状态,正洗时间一般设定为1~2分钟,正洗时间可通过调节操作面板14调整;When entering the working state of "washing", the
步骤二:到达正洗设定时间后,驱动控制器13驱动阀芯转动至“过滤”位置,阀体进水口A仍和外腔接口D相通,出水口B和内腔接口E相通,排污口C处于关闭截止状态;Step 2: After reaching the set time for positive washing, the
此时,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由外腔接口D,进入叠片式滤芯12和过滤器外壳之间,在流体压力作用下,液体穿透过滤碟片,进入滤芯内部,固体杂质或悬浮物被过滤碟片拦截;At this time, the effluent from the secondary settling tank flows in through the filter inlet A after being pressurized. Under the diversion of the
经由滤芯过滤后的清水经由内腔接口E,从出水口B流出,此时,过滤器处于“过滤”工作状态;The clean water filtered by the filter element flows out from the water outlet B through the inner cavity interface E. At this time, the filter is in the "filtering" working state;
在进入“过滤”工作状态时,驱动控制器13开始计时,随着过滤的进行,固体杂质不断被拦截、堆积,造成过滤阻力增大,差压升高,过滤效率降低,需要进入反洗状态对滤芯进行反洗;When entering the working state of "filtering", the
所述的步骤二中:进入反洗状态有三种控制方式,第一种是时间控制,到达过滤设定时间后,自动切换至反洗状态,过滤时间可通过调节操作面板14调整,控制器也可接受外部差压信号或流量信号,设定为差压控制模式或流量控制模式。In the second step: there are three control methods for entering the backwashing state. The first is time control. After reaching the filtering set time, it will automatically switch to the backwashing state. The filtering time can be adjusted by adjusting the
步骤三:在接收到反洗需求信号后,驱动控制器13驱动阀芯转动至“反洗”位置,阀体进水口A和内腔接口E相通,排污口C和外腔接口D相通,出水口B处于关闭截止状态;Step 3: After receiving the backwash demand signal, the
此时,二沉池出水通过加压后由过滤器进水口A流入,在导流件6的导流下,经由内腔接口E进入滤芯内部,在流体压力作用下,压紧过滤碟片4的压紧弹簧8被压缩,重叠的碟片放松,冲洗水穿过碟片间的缝隙进入过滤器腔体,固体杂质或悬浮物经由外腔接口D从排污口排出,从而使碟片可过滤器得到反冲洗;At this time, the effluent of the secondary sedimentation tank flows into the filter inlet A after being pressurized, and enters the filter element through the inner cavity interface E under the diversion of the
由于碟片两面刻有与中心线呈一定角度的放射状V型过滤通道,在冲洗水的压力作用下,碟片产生震动与旋转,碟片上的污物被离心力甩出,水在过滤器腔体形成旋流,腔体内污物被快速清扫排出,所以本装置反冲洗极为高效快速,在几秒至几十秒内完成反冲洗过程,反洗时间可通过调节操作面板14调整;Because the two sides of the disc are engraved with radial V-shaped filter channels at a certain angle to the center line, under the pressure of the flushing water, the disc vibrates and rotates, the dirt on the disc is thrown out by centrifugal force, and the water is in the filter cavity. The body forms a swirling flow, and the dirt in the cavity is quickly cleaned and discharged, so the backwashing of the device is extremely efficient and fast, and the backwashing process is completed within a few seconds to tens of seconds, and the backwashing time can be adjusted by adjusting the
反洗到达设定时间后,又切换至正洗状态,为下一次过滤做准备,周而复始,从而实现过滤器的全自动自清洗和过滤过程。After the backwash reaches the set time, it switches to the normal washing state again to prepare for the next filtration, and repeats the cycle, so as to realize the automatic self-cleaning and filtration process of the filter.
如上所述,自清洗过滤器的过滤碟片4两边刻有大量一定微米尺寸的V型沟槽,若干碟片叠压在支架7上,碟片间沟槽交叉,从而形成一系列独特过滤通道的深层过滤单元,过滤时碟片通过弹簧8和水流压力压紧,差压越大,压紧力越强,保证了自锁性高效过滤。反洗时,在水压反向作用下,压紧弹簧被顶开,碟片间形成缝隙,从而使每片碟片都得到充分清洗。As mentioned above, the
如上所述,本装置反洗亦利用过滤加压泵,用滤前水实现自清洗,不需要另设反冲洗水泵和冲洗水池,系统构成简单,过滤前的正洗过程保证了滤前水不会进入到过滤后的清水系统中,适用于污水深度处理的场合,也可用于循环水处理和中水回用中类似场景,适用性广泛。As mentioned above, the backwashing of this device also utilizes a filtration pressure pump, and uses the water before filtration to achieve self-cleaning, without the need for additional backwashing pumps and flushing pools, the system has a simple structure, and the positive washing process before filtration ensures that the water before filtration does not It will enter the filtered clean water system, and is suitable for the occasion of advanced sewage treatment. It can also be used in similar scenarios in circulating water treatment and reclaimed water reuse, and has a wide range of applicability.
如上所述,本装置过滤控制阀和过滤器高度集成,一阀实现正洗、过滤、反洗全过程,外部没有任何反洗管路,体积小,重量轻,方便与一体化污水处理设备配套集成。As mentioned above, the filtration control valve and filter of this device are highly integrated. One valve realizes the whole process of forward washing, filtration and backwashing. There is no external backwashing pipeline. It is small in size and light in weight, which is convenient for matching with integrated sewage treatment equipment. integrated.
如上所述,本装置的过滤控制阀和过滤器本体均用耐腐蚀高强度塑料材料制成,耐腐蚀,那酸碱,可适用于污水处理、工业废水处理、循环水处理、中水回用等场合使用。As mentioned above, the filter control valve and the filter body of the device are made of corrosion-resistant high-strength plastic materials, which are resistant to corrosion, acid and alkali, and can be applied to sewage treatment, industrial wastewater treatment, circulating water treatment, and reclaimed water reuse. Use in other occasions.
本发明具有以下优点:1、具有稳定的过滤效率,精确的过滤效果。独特的碟片设计、微米级过滤精度,确保只有粒径小于要求的颗粒才能进入系统,是最有效的过滤系统,用户可根据要求选择不同精度的过滤盘,过滤精度5~200μm范围内可供选择;2、本发明具有结构集成度高,占地小。采用模块化设计,结构集成度高,占地极小,没有任何传统过滤器复杂的外部反洗管道,同样过滤流量下,本装置体积仅约为传统砂滤的十分之一,重量仅为其二十分之一,可以很方便的装入一体化污水处理设备内部;3、独特的控制阀结构,一阀实现过滤和反洗全自动控制。采用特殊设计的三位五通电动转阀,通过阀芯的不同旋转位置,配合过滤器的流道结构,用一个控制阀取代传统过滤器四个电动阀才能实现的过滤、反冲洗、正冲洗功能;4、高效的反冲洗性能,反冲洗时节能节水。本发明具有极高的反冲洗性能,装置在过滤、反洗、正洗状态之间自动切换,只需几十秒就可完成反冲洗,反洗耗水量极少,占出水量的0.5%以下;5、不需设置反冲洗水泵,投资少。本发明不需要专用反冲洗水泵,而是通过控制阀的切换,利用过滤给水泵实现反冲洗,系统简单,投资低;6、耐腐蚀性能好,使用寿命长:控制阀、过滤元件及外壳均采用新型塑料材质制作,耐腐蚀、耐老化、无堵塞,过滤和反洗效果不会因使用时间而变差。The invention has the following advantages: 1. It has stable filtering efficiency and accurate filtering effect. The unique disc design and micron-level filtration precision ensure that only particles with a particle size smaller than the required size can enter the system. It is the most effective filtration system. Users can choose different precision filter discs according to their requirements. Option; 2. The present invention has high structural integration and small footprint. Modular design is adopted, the structure is highly integrated, and the floor area is extremely small. There is no complicated external backwashing pipeline of traditional filters. Under the same filtering flow, the volume of the device is only about one-tenth of the traditional sand filter, and the weight is only One twentieth of it can be easily installed into the integrated sewage treatment equipment; 3. Unique control valve structure, one valve realizes automatic control of filtration and backwashing. Using a specially designed three-position five-way electric rotary valve, through the different rotation positions of the valve core and the flow channel structure of the filter, a control valve is used to replace the four electric valves of the traditional filter. Function; 4. Efficient backwashing performance, energy saving and water saving during backwashing. The invention has extremely high backwashing performance, the device automatically switches between the states of filtration, backwashing and normal washing, and the backwashing can be completed in only tens of seconds, and the backwashing water consumption is extremely small, accounting for less than 0.5% of the water output. 5. There is no need to set up a backwash pump, and the investment is small. The invention does not need a special backwash pump, but uses the filter feed pump to realize backwash through the switching of the control valve, the system is simple, and the investment is low; 6. Good corrosion resistance and long service life: the control valve, filter element and shell are all Made of new plastic material, it is corrosion-resistant, aging-resistant, non-clogging, and the filtering and backwashing effects will not deteriorate due to use time.
对于污水处理排放标准要求日益严苛的当下,作为二级污水处理系统出水的后端深度处理装置,该发明具有广阔的应用前景。以上实施案例对于本发明进行了详细说明,但所述内容仅为本发明的优选实施方式,但本发明并不限于上述实施方式,在所述领域普通技术人员所具备的知识范围内,本发明的精神和原则之内所作的任何修改、等同替代及改进等,均应视为本申请的保护范围。With the increasingly stringent requirements of sewage treatment and discharge standards, the invention has broad application prospects as a back-end advanced treatment device for the effluent of the secondary sewage treatment system. The above embodiments have described the present invention in detail, but the content is only the preferred embodiment of the present invention, but the present invention is not limited to the above-mentioned embodiment, within the scope of knowledge possessed by those of ordinary skill in the field, the present invention Any modifications, equivalent substitutions and improvements made within the spirit and principles of the present application shall be deemed as the protection scope of this application.
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