CN103663820A - Air flotation membrane filtration purification system - Google Patents
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Abstract
Description
技术领域 technical field
本发明涉及一种净水处理厂以及中水回用水厂水质处理装置,特别提供了一种气浮膜滤净化系统。 The invention relates to a water quality treatment device for a water purification treatment plant and a reclaimed water reuse plant, and in particular provides an air flotation membrane filtration purification system. the
背景技术 Background technique
目前,当净水厂水源浊度较低或藻类较高时,常采用气浮加过滤的技术。现有的水厂常修建单独的气浮池,采用部分回流溶气气浮法,气浮池的气浮分离区底部设穿孔集水管集水,上部为空池,空间浪费严重。气浮后过滤工艺常采用砂滤池或超滤膜过滤,砂滤池土建结构相对复杂,占地面积大,滤池必须定期反洗,反洗耗水量大,运行成本高。超滤膜净水处理技术作为一种新型技术在水处理领域应用越来越广,可以直接取代砂滤池作为最后的处理系统。传统的超滤膜过滤技术,管路、阀门过多,控制复杂,维护麻烦,系统容易漏水,占地面积较大。现在逐渐发展应用的浸没式膜过滤技术,将超滤膜做成若干个组件放置在一池体内,但是存在着抗负荷能力小,反冲洗后需要将池内水全部排掉,造成自用水率偏高等缺点。 At present, when the turbidity of the water source of the water purification plant is low or the algae is high, the technology of air flotation and filtration is often used. Existing water plants often build separate air flotation tanks, using the partial reflux dissolved air flotation method. The bottom of the air flotation separation zone of the air flotation tank is equipped with a perforated water collection pipe to collect water, and the upper part is an empty tank, which is a serious waste of space. The filtration process after air flotation often adopts sand filter or ultrafiltration membrane filtration. The civil structure of the sand filter is relatively complex and occupies a large area. The filter must be backwashed regularly, which consumes a lot of water and high operating costs. As a new type of technology, ultrafiltration membrane water purification treatment technology is more and more widely used in the field of water treatment, and can directly replace sand filters as the final treatment system. The traditional ultrafiltration membrane filtration technology has too many pipelines and valves, complicated control, troublesome maintenance, easy leakage of the system, and a large footprint. Now the submerged membrane filtration technology is gradually developed and applied. The ultrafiltration membrane is made into several components and placed in a pool, but there is a small load resistance capacity. High disadvantage. the
发明内容 Contents of the invention
本发明针对上述技术问题,提出一种用于处理低浊或高藻水,同时占地面积小,结构简单,土建造价低,抗负荷能力大,自用水率低,控制简单的气浮膜滤净化系统。 Aiming at the above technical problems, the present invention proposes an air flotation membrane filter for treating low-turbidity or high-algae water with small footprint, simple structure, low civil construction cost, high load resistance capacity, low self-water rate, and simple control. purification system. the
为达到以上目的,通过以下技术方案实现的: In order to achieve the above purpose, it is achieved through the following technical solutions:
气浮膜滤净化系统,包括:由外墙体围成的过滤池本体,溶气气浮装置和设置于过滤池本体内部的浸没式膜过滤装置; The air flotation membrane filtration purification system includes: the filter tank body surrounded by the outer wall, the dissolved air flotation device and the submerged membrane filter device installed inside the filter tank body;
过滤池本体内部由隔墙将过滤池本体内池分成进水缓冲区,进水配水区,气浮接触区,气浮分离区兼膜过滤出水区; The interior of the filter body is divided into water inlet buffer zone, water inlet water distribution area, air flotation contact area, air flotation separation area and membrane filter water outlet area by the partition wall;
进水缓冲区与进水配水区中间间隔为进水配水堰; The middle interval between the water inlet buffer zone and the water inlet distribution area is the water inlet distribution weir;
过滤池本体外壁设置有用于与进水缓冲区连通的进水管; The outer wall of the filter body is provided with a water inlet pipe for communicating with the water inlet buffer zone;
进水配水区与气浮接触区通过设置于进水配水区与气浮接触区之间隔墙的进水配水孔连通; The water inlet distribution area and the air flotation contact area are connected through the water inlet distribution hole set in the partition wall between the water inlet water distribution area and the air flotation contact area;
溶气气浮装置包括:用于输出溶气水的溶气泵或溶气罐,用于导向溶气水 的溶气水输送管道和用于产生微气泡的微气泡发生装置; The dissolved air flotation device includes: a dissolved air pump or dissolved air tank for outputting dissolved air water, a dissolved air water delivery pipeline for guiding dissolved air water and a microbubble generating device for generating microbubbles;
溶气水输送管道固定于加工有进水配水孔的隔墙上,且一端与溶气泵或溶气罐的输出端固定,另一端伸入于气浮接触区内部; The dissolved air water delivery pipeline is fixed on the partition wall processed with water inlet and distribution holes, and one end is fixed to the output end of the dissolved air pump or dissolved air tank, and the other end extends into the air flotation contact area;
微气泡发生装置固定于溶气水输送管道伸入于气浮接触区端部; The microbubble generating device is fixed on the dissolved air water delivery pipeline and extends into the end of the air flotation contact area;
过滤池本体气浮分离区兼膜过滤出水区池底加工有若干横截面为向下凸起的锥状泥斗;锥状泥斗下端设置有排泥管; In the air flotation separation area of the filter body and the membrane filtration water outlet area, the bottom of the pool is processed with a number of conical mud buckets with a downwardly convex cross section; the lower end of the conical mud bucket is provided with a mud discharge pipe;
浸没式膜过滤装置包括:通过不锈钢框架设置于过滤池本体气浮分离区兼膜过滤出水区内部的浸没式膜组件、浸没式膜出水总管和浸没式膜反洗进气总管; The submerged membrane filtration device includes: the submerged membrane module, the submerged membrane outlet main pipe and the submerged membrane backwash inlet main pipe which are arranged in the air flotation separation area of the filter body and the membrane filtration water outlet area through a stainless steel frame;
浸没式膜出水总管兼做浸没式膜进水总管,且一端与浸没式膜组件各浸没式膜出水支管连通,另一端与抽吸泵连通; The submerged membrane outlet main pipe is also used as the submerged membrane water inlet main pipe, and one end is connected with each submerged membrane outlet branch pipe of the submerged membrane module, and the other end is connected with the suction pump;
浸没式膜反洗进气总管一端与浸没式膜组件各浸没式膜反洗进气支管连通,另一端与鼓风机连通; One end of the submerged membrane backwash intake manifold is connected to each submerged membrane backwash intake branch pipe of the submerged membrane module, and the other end is connected to the blower;
过滤池本体上设置有通过管路与浸没式膜组件各个浸没式膜出水支管连通的药洗总管; The main body of the filter tank is provided with a medicine washing main pipe that communicates with each submerged membrane outlet branch pipe of the submerged membrane module through pipelines;
过滤池本体上端设置有用于刮除表面浮渣的刮渣行走机构; The upper end of the filter tank body is provided with a scraper walking mechanism for scraping off surface scum;
过滤池本体位于刮渣行走机构行程末端设置有排渣槽; The filter tank body is located at the end of the stroke of the slag scraping mechanism, and a slag discharge groove is installed;
排渣槽与气浮分离区兼膜过滤出水区连接处由排渣堰隔开; The connection between the slag discharge tank and the air flotation separation area and membrane filtration water area is separated by a slag discharge weir;
过滤池本体气浮分离区兼膜过滤出水区内部设置有用于加强支撑浸没式膜组件不锈钢框架的支撑梁; The air flotation separation area of the filter body and the membrane filtration water outlet area are equipped with support beams for strengthening the support of the stainless steel frame of the submerged membrane module;
刮渣行走机构装配于过滤池本体侧壁布置的轨道上行走,且由电机驱动行走;排渣槽设置于与过滤池本体进水口相对端; The slag-scraping walking mechanism is assembled on the track arranged on the side wall of the filter tank body and driven by a motor; the slag discharge tank is set at the opposite end to the water inlet of the filter tank body;
排渣槽设置有用于冲刷排渣槽的冲洗水管; The slag discharge tank is provided with a flushing water pipe for flushing the slag discharge tank;
作为优选,浸没式膜组件根据出水水质的要求,采用超滤膜,或者微孔过滤膜; As a preference, the submerged membrane module adopts ultrafiltration membrane or microporous filtration membrane according to the requirements of effluent water quality;
作为优选,浸没式膜组件通过药洗总管注入次氯酸钠溶液进行药洗; As a preference, the submerged membrane module injects sodium hypochlorite solution through the medicine washing main pipe for medicine washing;
作为优选,浸没式膜组件上淹没水深1-2米; As a preference, the submerged water depth of the submerged membrane module is 1-2 meters;
作为优选,各个排泥管连通串联在一起,且在排泥管上安装有可自动控制阀门和手动阀门; As a preference, each mud discharge pipe is connected in series, and an automatic control valve and a manual valve are installed on the mud discharge pipe;
当处理水量大时,过滤池本体为混凝土浇筑结构,当处理水量较小时,过滤池本体可做成一种外壳材质为金属或塑料的小型净水处理设备; When the amount of treated water is large, the filter body is a concrete pouring structure. When the amount of treated water is small, the filter body can be made into a small water purification treatment equipment with a metal or plastic shell;
采用上述技术方案的本发明事先需装配控制柜,且控制柜中设置有可编程序控制器(简称PLC)完成固定程序的存储及执行,以及装配于控制柜表面用于进行人工设置参数及操作的人机界面HMI; The present invention adopting the above-mentioned technical solution needs to assemble a control cabinet in advance, and the control cabinet is provided with a programmable logic controller (abbreviated as PLC) to complete the storage and execution of the fixed program, and is assembled on the surface of the control cabinet for manual setting of parameters and operation Human-machine interface HMI;
气浮膜滤净化系统的控制方法,包括以下步骤: The control method of the air flotation membrane filtration purification system comprises the following steps:
步骤一,在需过滤水和溶气水共同注入过程中,检测气浮分离区兼膜过滤出水区水位液面,当水位液面到达指定高度启动浸没式膜出水总管出水泵实现过滤水排出; Step 1. During the co-injection of filtered water and dissolved air water, detect the water level in the air flotation separation area and the membrane filtration water outlet area, and when the water level reaches the specified height, start the submerged membrane water outlet main pipe outlet pump to discharge the filtered water;
上述操作步骤之前,需要在进水管上装配进水电控阀门,浸没式膜出水总管出口端与转子泵连通,设置液位计监测气浮分离区兼膜过滤出水区水位液面高度,且进水电控阀门、转子泵和液位计都通过电路与控制柜连通; Before the above operation steps, it is necessary to assemble the water inlet electric control valve on the water inlet pipe, the outlet end of the submerged membrane outlet main pipe is connected with the rotor pump, and the liquid level gauge is set to monitor the water level in the air flotation separation area and the membrane filtration water outlet area, and enter Water electric control valves, rotor pumps and liquid level gauges are all connected to the control cabinet through circuits;
溶气水进水可通过自动空压机、回流泵等溶气部分设备实现,这部分设备也可以完全通过一个溶气泵设备来实现,且都通过电路与控制柜连通; Dissolved air water inflow can be realized through automatic air compressor, return pump and other dissolved air equipment, and this part of equipment can also be completely realized through a dissolved air pump equipment, and all of them are connected with the control cabinet through the circuit;
具体控制,首先人机界面HMI设定液位计监测指定液面高度,当液面高度低于指定液面高度时,液位计发出低液位信号至可编程序控制器(简称PLC)进行比较,然后发出低液位执行指令,控制溶气水进水设备与进水电控阀门工作实现注入溶气水和需过滤水,当液位计监测液面高度达到指定高度,此时液位计发出正常工作信号至可编程序控制器(简称PLC)进行比较然后发出正常运作执行指令,控制溶气水进水设备与进水电控阀门来控制溶气水和需过滤水的总注入量,同时控制启动转子泵吸出过滤水,总体液面通过液位计实时监测,通过可编程序控制器(简称PLC)进行控制调控; For specific control, firstly, the human-machine interface HMI sets the liquid level gauge to monitor the specified liquid level height. When the liquid level height is lower than the specified liquid level height, the liquid level gauge sends a low liquid level signal to the programmable logic controller (PLC for short). Compare, and then issue a low liquid level execution command to control the dissolved air water inlet equipment and the water inlet electric control valve to inject dissolved air water and water to be filtered. When the liquid level gauge monitors the liquid level to reach the specified height, the liquid level The meter sends a normal working signal to the programmable logic controller (abbreviated as PLC) for comparison and then sends out a normal operation execution command to control the dissolved air water inlet equipment and water inlet electric control valve to control the total injection volume of dissolved air water and water to be filtered , and at the same time control and start the rotor pump to suck out the filtered water, the overall liquid level is monitored in real time by the liquid level gauge, and controlled and regulated by the programmable logic controller (PLC for short);
步骤二,排渣,在气浮膜滤净化系统运行一定的时间后,对气浮膜滤净化系统滤池表面渣滓刮除、排掉;首先控制加大进水量,减少出水量来抬高气浮膜滤净化系统滤池表面液位高度,然后启动刮渣行走机构行走刮渣;渣滓刮除排放入排渣槽内,然后通过冲洗水管冲洗排出;排渣过程结束后气浮膜滤净化系统恢复正常运行;
刮渣行走机构可为,行走小车滚轮直接通过电机驱动行走于过滤池本体侧壁布置的轨道上,且电机与控制柜通过电路连通; The slag scraping walking mechanism can be that the rollers of the trolley are directly driven by the motor to walk on the track arranged on the side wall of the filter tank body, and the motor and the control cabinet are connected through a circuit;
排渣为定时执行过程,定时时间长度由整个液面渣滓形成速率来决定,首先控制柜内部设置刮渣定时器,通过人机界面HMI来设定一个定时时间值,当到达定时时间值时刮渣定时器发出刮渣信号至可编程序控制器(简称PLC),然后可编程序控制器(简称PLC)同时输出控制增加溶气水和需过滤水总注入量, 减少出水量,以抬高液面,然后控制启动刮渣行走机构电机驱动行走,刮渣行走机构到气浮分离区兼膜过滤出水区排渣端时,需要将刮渣行走机构下端排渣板展开一定的角度,然后继续行走进行排渣,渣滓刮除排放入排渣槽内,然后通过冲洗水管冲洗排出;排渣完成后可编程序控制器(简称PLC)控制溶气水和需过滤水总注入量以及出水量,使液面总体恢复,本系统继续正常运行; Slag discharge is a timing execution process, and the length of timing is determined by the formation rate of dross on the entire liquid surface. First, a scraping timer is set inside the control cabinet, and a timing value is set through the man-machine interface HMI. When the timing value is reached, the scraping time is reached. The slag timer sends a slag scraping signal to the programmable logic controller (referred to as PLC), and then the programmable controller (abbreviated as PLC) simultaneously outputs control to increase the total injection volume of dissolved air water and water to be filtered, and reduce the water output to increase Then control and start the slag scraping mechanism to drive the motor. When the slag scraping mechanism reaches the slag discharge end of the air flotation separation area and membrane filtration water outlet area, it is necessary to unfold the slag discharge plate at the lower end of the slag scraping mechanism at a certain angle, and then continue The slag is discharged by walking, and the slag is scraped and discharged into the slag discharge tank, and then washed and discharged through the flushing water pipe; after the slag discharge is completed, the programmable logic controller (PLC) controls the total injection volume and water output of dissolved air water and filtered water, The liquid level is generally restored, and the system continues to operate normally;
步骤三,排泥,在气浮膜滤净化系统运行一定的时间后,对气浮膜滤净化系统沉积于锥状泥斗的沉积物,然后通过排泥管排出,气浮膜滤净化系统的排泥频率由气浮膜滤净化系统沉积率决定;
排泥同样为定时执行过程,定时时间长度由本过滤池本体底部锥状泥斗淤泥形成速率决定; Sludge discharge is also a timing process, and the timing length is determined by the sludge formation rate of the cone-shaped mud bucket at the bottom of the filter body;
排泥控制分为两种一种为手动通过设置于排泥管上的手动阀门控制排出,或者在控制柜内部设置排泥定时器,通过人机界面HMI来设定一个定时时间值,当到达定时时间值时排泥定时器发出排泥信号至可编程序控制器(简称PLC),然后可编程序控制器(简称PLC)输出控制排泥管上的自动控制阀门打开,实现排泥操作;排泥操作过程不影响过滤程序运行; There are two kinds of mud discharge control: one is to manually control the discharge through the manual valve installed on the mud discharge pipe, or set a mud discharge timer inside the control cabinet, and set a timing value through the man-machine interface HMI. When the time is set, the mud discharge timer sends a mud discharge signal to the programmable logic controller (abbreviated as PLC), and then the programmable logic controller (abbreviated as PLC) outputs to control the opening of the automatic control valve on the mud discharge pipe to realize the mud discharge operation; The sludge discharge operation does not affect the operation of the filtration program;
步骤四,反洗过程,浸没式膜组件运行一段时间后需要反洗,反洗时浸没式膜出水总管出口端的转子泵变成将净水打入浸没式膜内部,将附着在膜孔隙及表面的污染物冲洗下来,为了保证反洗效果,在水洗的同时还通过与浸没式膜反洗进气总管连通的鼓风机鼓气进行气洗,反洗完毕静止一段时间后,水中的污染物沉积到滤池底部的锥形泥斗内,再通过排泥管排到池外,通过排泥管的自动控制阀门实现,可通过远程控制,手动阀门在自动控制阀门需要检修时可用,浸没式膜组件每隔一定周期还需要进行药洗,药洗是将次氯酸钠溶液通过药洗总管注入浸没式膜出水支管分向各浸没式膜组件,药洗完毕后将池内水通过排泥管全部排掉。
控制柜在完成上述控制过程的同时,实时监控,每个电动设备状态时刻记录在控制柜中,出现异常及时控制预先配置的声光报警装置报警。 While the control cabinet completes the above control process, it monitors in real time, records the status of each electric equipment in the control cabinet at all times, and promptly controls the pre-configured sound and light alarm device to alarm in case of abnormality. the
综上,本发明与传统工艺比较具有以下优点: In summary, the present invention has the following advantages compared with traditional techniques:
第一,气浮膜滤净化系统将气浮工艺和膜过滤工艺有机结合,气浮分离与膜过滤在同一个池子里完成,充分利用了气浮池分离区的空间,不用另外修建池子,节省占地面积及造价;以相同处理量的万吨水厂为例,若按传统气浮加砂滤池工艺设计,气浮出水接砂滤池,设计滤速7m/h,则净过滤面积需要60平 方米,加上砂滤池前后进出水区及结构墙,需在气浮膜滤池占地面积基础上至少增加约100平方米的面积用来修建滤池;若按传统气浮加超滤膜工艺设计,采用外径160mm的超滤膜,单只产水量1t/h,则需要670根膜,将这些膜及配套管道布置下来,需在气浮膜滤净化系统占地面积基础上至少增加约200平方米的面积。 First, the air flotation membrane filtration purification system organically combines the air flotation process and the membrane filtration process, and the air flotation separation and membrane filtration are completed in the same pool, which makes full use of the space in the separation area of the air flotation pool, and does not need to build another pool, saving the occupied area. Land area and cost; taking a 10,000-ton water plant with the same treatment capacity as an example, if the traditional air flotation and sand filter process is designed, the air flotation outlet is connected to the sand filter, and the design filtration rate is 7m/h, the net filtration area needs 60 square meters, plus the water inlet and outlet areas and structural walls before and after the sand filter, it is necessary to increase the area of at least about 100 square meters on the basis of the area occupied by the air flotation membrane filter to build the filter; The ultrafiltration membrane process design uses an ultrafiltration membrane with an outer diameter of 160mm, and a single water production rate of 1t/h requires 670 membranes. To arrange these membranes and supporting pipelines, it needs to be based on the area occupied by the air flotation membrane filtration purification system. At least increase the area of about 200 square meters. the
第二,气浮膜滤净化系统将气浮分离作为膜过滤处理的预处理,能提高膜过滤处理的抗负荷能力,同时气浮产生的微气泡对浸没式膜组件的膜丝表面有摩擦清洗作用,能提高膜的抗污染性,而反过来膜过滤处理出水代替气浮传统的集水槽或穿孔管集水出水方式,又能大幅提高气浮处理的出水水质;气浮膜滤净化系统内膜组件过滤精度高,能保证最后出水浊度在0.2NTU以下,而砂滤池随过滤时间的增长,若反洗不及时,很容易存在滤池穿透现象,出水浊度无法保证在1NTU以下,气浮膜滤净化系统出水水质明显优于砂滤池。 Second, the air flotation membrane filtration purification system uses air flotation separation as the pretreatment of the membrane filtration treatment, which can improve the load resistance of the membrane filtration treatment, and at the same time, the microbubbles generated by the air flotation can frictionally clean the surface of the membrane filaments of the submerged membrane module The function can improve the anti-pollution of the membrane, and in turn, membrane filtration can replace the traditional water collection tank or perforated pipe water collection and discharge method of air flotation, and can greatly improve the effluent water quality of air flotation treatment; the air flotation membrane filtration purification system Membrane modules have high filtration precision and can ensure that the turbidity of the final effluent is below 0.2NTU. However, with the increase of the filtration time of the sand filter, if the backwashing is not timely, it is easy to have filter penetration, and the turbidity of the effluent cannot be guaranteed to be below 1NTU. , The effluent quality of the air flotation membrane filtration purification system is obviously better than that of the sand filter. the
第三,气浮膜滤净化系统在池子底部设置多个锥形泥斗,对池内膜组件进行反洗的过程中产生的污染物,经过重力静沉落入泥斗内,通过串联各泥斗的排泥管排向池外,不用将整个池子的水排掉,降低了水厂的自用水率;第四,气浮膜滤净化系统反冲洗周期短、时间短、用水量小。相同处理量的万吨水厂,气浮膜滤净化系统一次反冲洗时间是砂滤池的十分之一,消耗水量是砂滤池的七分之一,反冲洗周期比超滤膜反冲洗周期延长1倍以上。 Thirdly, the air flotation membrane filtration purification system sets multiple conical mud hoppers at the bottom of the pool. The mud discharge pipe of the bucket is discharged out of the pool, without draining the water of the entire pool, which reduces the self-water rate of the water plant; fourth, the backwash cycle of the air flotation membrane filtration purification system is short, the time is short, and the water consumption is small. For a 10,000-ton water plant with the same processing capacity, the backwashing time of the air flotation membrane filtration purification system is one-tenth of that of the sand filter, the water consumption is one-seventh of the sand filter, and the backwashing cycle is shorter than that of the ultrafiltration membrane. The period is more than doubled. the
第五,气浮膜滤净化系统膜组件安装简单,维修方便。相同处理量的万吨水厂,施工工期比超滤膜缩短5天左右,安装材料比超滤膜减少20%。 Fifth, the membrane components of the air flotation membrane filtration purification system are easy to install and easy to maintain. For a 10,000-ton water plant with the same treatment capacity, the construction period is about 5 days shorter than that of ultrafiltration membranes, and the installation materials are 20% less than that of ultrafiltration membranes. the
第六,气浮膜滤净化系统只需要一台泵即可实现产水与反洗功能,而超滤膜需要两台泵来实现。 Sixth, the air flotation membrane filtration purification system only needs one pump to realize the functions of water production and backwashing, while the ultrafiltration membrane needs two pumps to realize it. the
第七,气浮膜滤净化系统控制装置自动完成气浮膜滤净化系统的工艺自动操作,大大减少了人为操作,提高了劳动生产力。 Seventh, the control device of the air flotation membrane filtration purification system automatically completes the process automatic operation of the air flotation membrane filtration purification system, which greatly reduces human operations and improves labor productivity. the
本发明简化了气浮过滤工艺的生产管理流程,节省了占地面积,减少了投资和运行费用,节约成本。 The invention simplifies the production and management process of the air flotation filtration process, saves the occupied area, reduces the investment and operating expenses, and saves the cost. the
上述说明仅是本发明技术方案的概述,为了能够更清楚了解本发明的技术手段,而可依照说明书的内容予以实施,并且为了让本发明的上述和其他目的、特征和优点能够更明显易懂,以下特举较佳实施例,并配合附图,详细说明如下。 The above description is only an overview of the technical solution of the present invention. In order to better understand the technical means of the present invention, it can be implemented according to the contents of the description, and in order to make the above and other purposes, features and advantages of the present invention more obvious and understandable , the following preferred embodiments are specifically cited below, and are described in detail as follows in conjunction with the accompanying drawings. the
附图说明 Description of drawings
本发明共4幅附图,其中: The present invention has 4 drawings in total, in which:
图1为本发明的上部横向剖面结构示意图。 Fig. 1 is a schematic view of the upper transverse cross-sectional structure of the present invention. the
图2为本发明的下部横向剖面结构示意图。 Fig. 2 is a schematic view of the lower transverse cross-sectional structure of the present invention. the
图3为图1A-A位置纵向剖面结构示意图。 Fig. 3 is a schematic diagram of a longitudinal section structure at the position of Fig. 1A-A. the
图4为本发明的气浮膜滤净化系统及其控制系统示意图。 Fig. 4 is a schematic diagram of the air flotation membrane filtration purification system and its control system of the present invention. the
具体实施方式 Detailed ways
如图1、图2、图3和图4所示的气浮膜滤净化系统,包括:由外墙体围成的过滤池本体27,溶气气浮装置28和设置于过滤池本体27内部的浸没式膜过滤装置29;
The air flotation membrane filtration purification system shown in Fig. 1, Fig. 2, Fig. 3 and Fig. 4 includes: a
过滤池本体27内部由隔墙将过滤池本体27内池分成进水缓冲区2,进水配水区4,气浮接触区6,气浮分离区兼膜过滤出水区7;
The inner pool of the
进水缓冲区2与进水配水区4中间间隔为进水配水堰3;
The middle interval between the
过滤池本体27外壁设置有用于与进水缓冲区2连通的进水管1;
The outer wall of the
进水配水区4与气浮接触区6通过设置于进水配水区4与气浮接触区6之间隔墙的进水配水孔5连通;
The water
溶气气浮装置28包括:用于输出溶气水的溶气泵或溶气罐,用于导向溶气水的溶气水输送管道20和用于产生微气泡的微气泡发生装置21;
The dissolved
溶气水输送管道20固定于加工有进水配水孔5的隔墙上,且一端与溶气泵或溶气罐的输出端固定,另一端伸入于气浮接触区6内部;
The dissolved air
微气泡发生装置21固定于溶气水输送管道20伸入于气浮接触区6端部;
The
过滤池本体27气浮分离区兼膜过滤出水区7池底加工有若干横截面为向下凸起的锥状泥斗22;锥状泥斗22下端设置有排泥管23;
The
浸没式膜过滤装置29包括:通过不锈钢框架8设置于过滤池本体27气浮分离区兼膜过滤出水区7内部的浸没式膜组件9、浸没式膜出水总管12和浸没式膜反洗进气总管13;
The submerged
浸没式膜出水总管12兼做浸没式膜进水总管,且一端与浸没式膜组件9各浸没式膜出水支管10连通,另一端与抽吸泵连通;
The submerged membrane water outlet
浸没式膜反洗进气总管13一端与浸没式膜组件9各浸没式膜反洗进气支管11连通,另一端与鼓风机连通;
One end of the submerged membrane
过滤池本体27上设置有通过管路与浸没式膜组件9各个浸没式膜出水支管10连通的药洗总管15;
The
过滤池本体27上端设置有用于刮除表面浮渣的刮渣行走机构19;
The upper end of the
过滤池本体27位于刮渣行走机构19行程末端设置有排渣槽17;
The
排渣槽17与气浮分离区兼膜过滤出水区7连接处由排渣堰18隔开;
The connection between the
过滤池本体27气浮分离区兼膜过滤出水区7内部设置有用于加强支撑浸没式膜组件9不锈钢框架8的支撑梁26;即不锈钢框架8坐落于气浮分离区兼膜过滤出水区7内的支撑梁26;
The
刮渣行走机构19装配于过滤池本体27侧壁布置的轨道上行走,且由电机驱动行走;刮渣行走机构19行走平面平行于排渣槽17上端平面并位于排渣槽17上端上方;
The slag-scraping
排渣槽17设置于与过滤池本体27进水口相对端;
The
排渣槽17设置有用于冲刷排渣槽17的冲洗水管16;
The
作为优选,浸没式膜组件9根据出水水质的要求,采用超滤膜,或者微孔过滤膜;
As preferably, submerged
作为优选,浸没式膜组件9通过药洗总管15注入次氯酸钠溶液进行药洗;
As preferably, submerged
作为优选,浸没式膜组件9上淹没水深1-2米;
As preferably, submerged water depth 1-2 meters on submerged
作为优选,各个排泥管23连通串联在一起,且在排泥管23上安装有可自动控制阀门和手动阀门;
As preferably, each
当处理水量大时,过滤池本体27为混凝土浇筑结构,当处理水量较小时,过滤池本体27可做成一种外壳材质为金属或塑料的小型净水处理设备;
When the amount of treated water is large, the
采用上述技术方案的本发明正常运行时,原水(需过滤水)由进水管1进入缓冲区2后通过配水区4及进水配水孔5均匀的进入气浮接触区6,溶气水输送管道20将溶气水输送过来,通过微气泡发生装置21释放出微气泡,微气泡与原水中悬浮颗粒在气浮接触区6内结合后进入气浮分离区兼浸没式膜过滤区7,悬浮颗粒被微气泡带着上浮聚集在气浮分离区兼浸没式膜过滤区7上部,定期由刮渣行走机构19刮至排渣槽17排出,浸没式膜组件9通过抽吸泵抽吸将水进一步过滤后产出。
When the present invention adopts the above-mentioned technical solution in normal operation, the raw water (water to be filtered) enters the
采用上述技术方案的本发明事先需装配控制柜33,且控制柜33中设置有可编程序控制器(简称PLC)完成固定程序的存储及执行,以及装配于控制柜33表面用于进行人工设置参数及操作的人机界面HMI32; The present invention adopting the above-mentioned technical solution needs to assemble a control cabinet 33 in advance, and a programmable logic controller (abbreviated as PLC) is arranged in the control cabinet 33 to complete the storage and execution of the fixed program, and is assembled on the surface of the control cabinet 33 for manual setting. Parameter and operation man-machine interface HMI32;
一种溶气气浮气膜式过滤系统的控制方法,包括以下步骤: A method for controlling a dissolved air flotation air membrane filter system, comprising the following steps:
步骤一,在需过滤水和溶气水共同注入过程中,检测气浮分离区兼膜过滤 出水区7水位液面,当水位液面到达指定高度启动浸没式膜出水总管12出水泵实现过滤水排出;
Step 1. During the joint injection of filtered water and dissolved air water, detect the water level in the air flotation separation zone and the membrane filtration
上述操作步骤之前,需要在进水管1上装配进水电控阀门,浸没式膜出水总管12出口端与转子泵连通,设置液位计30监测气浮分离区兼膜过滤出水区7水位液面高度,且进水电控阀门、转子泵和液位计30都通过电路与控制柜33连通;
Before the above operation steps, it is necessary to assemble the water inlet electric control valve on the water inlet pipe 1, the outlet end of the submerged membrane water outlet
溶气水进水可通过自动空压机、回流泵等溶气部分设备实现,这部分设备也可以完全通过一个溶气泵设备来实现,且都通过电路与控制柜33连通; The water inflow of dissolved air water can be realized through the automatic air compressor, return pump and other dissolved air equipment, and this part of equipment can also be completely realized through a dissolved air pump equipment, and all of them are connected with the control cabinet 33 through the circuit;
具体控制,首先人机界面HMI32设定液位计30监测指定液面高度,当液面高度低于指定液面高度时,液位计30发出低液位信号至可编程序控制器(简称PLC)进行比较,然后发出低液位执行指令,控制溶气水进水设备与进水电控阀门工作实现注入溶气水和需过滤水,当液位计30监测液面高度达到指定高度,此时液位计30发出正常工作信号至可编程序控制器(简称PLC)进行比较然后发出正常运作执行指令,控制溶气水进水设备与进水电控阀门来控制溶气水和需过滤水的总注入量,同时控制启动转子泵吸出过滤水,总体液面通过液位计30实时监测,通过可编程序控制器(简称PLC)进行控制调控;
Concrete control, at first the man-machine interface HMI32 sets the
步骤二,排渣,在一种溶气气浮气膜式过滤系统运行一定的时间后,对一种溶气气浮气膜式过滤系统滤池表面渣滓刮除、排掉;首先控制加大进水量,减少出水量来抬高一种溶气气浮气膜式过滤系统滤池表面液位高度,然后启动刮渣行走机构19行走刮渣;渣滓刮除排放入排渣槽17内,然后通过冲洗水管16冲洗排出;排渣过程结束后一种溶气气浮气膜式过滤系统恢复正常运行;
刮渣行走机构19可为,行走小车滚轮直接通过电机驱动行走于过滤池本体27侧壁布置的轨道上,且电机与控制柜33通过电路连通;
The slag
排渣为定时执行过程,定时时间长度由整个液面渣滓形成速率来决定,首先控制柜33内部设置刮渣定时器,通过人机界面HMI32来设定一个定时时间值,当到达定时时间值时刮渣定时器发出刮渣信号至可编程序控制器(简称PLC),然后可编程序控制器(简称PLC)同时输出控制增加溶气水和需过滤水总注入量,减少出水量,以抬高液面,然后控制启动刮渣行走机构19电机驱动行走,刮渣行走机构19到气浮分离区兼膜过滤出水区7排渣端时,需要将刮渣行走机构19下端排渣板31展开一定的角度,然后继续行走进行排渣,渣滓刮除排放入排渣槽17内,然后通过冲洗水管16冲洗排出;排渣完成后可编程序控制器(简 称PLC)控制溶气水和需过滤水总注入量以及出水量,使液面总体恢复,本系统继续正常运行;
The slag discharge is a timing execution process, and the timing length is determined by the dross formation rate of the entire liquid surface. First, a slag scraping timer is set inside the control cabinet 33, and a timing value is set through the man-machine interface HMI32. When the timing value is reached The slag scraping timer sends a slag scraping signal to the programmable logic controller (abbreviated as PLC), and then the programmable logic controller (abbreviated as PLC) simultaneously outputs control to increase the total injection volume of dissolved air water and water to be filtered, and reduce the water output to improve When the liquid level is high, then control and start the
步骤三,排泥,在一种溶气气浮气膜式过滤系统运行一定的时间后,对一种溶气气浮气膜式过滤系统沉积于锥状泥斗22的沉积物,然后通过排泥管23排出,一种溶气气浮气膜式过滤系统的排泥频率由一种溶气气浮气膜式过滤系统沉积率决定;
排泥同样为定时执行过程,定时时间长度由本过滤池本体27底部锥状泥斗22淤泥形成速率决定;
The mud discharge is also a timing execution process, and the timing length is determined by the sludge formation rate of the
排泥控制分为两种一种为手动通过设置于排泥管23上的手动阀门控制排出,或者在控制柜33内部设置排泥定时器,通过人机界面HMI32来设定一个定时时间值,当到达定时时间值时排泥定时器发出排泥信号至可编程序控制器(简称PLC),然后可编程序控制器(简称PLC)输出控制排泥管23上的自动控制阀门打开指令,实现排泥操作;排泥操作过程不影响过滤程序运行。
There are two types of mud discharge control: one is to manually control the discharge through the manual valve installed on the
步骤四,反洗过程,浸没式膜组件9运行一段时间后需要反洗,反洗时浸没式膜出水总管12出口端的转子泵变成将净水打入浸没式膜内部,将附着在膜孔隙及表面的污染物冲洗下来,为了保证反洗效果,在水洗的同时还通过与浸没式膜反洗进气总管13连通的鼓风机鼓气进行气洗,反洗完毕静止一段时间后,水中的污染物沉积到滤池底部的锥形泥斗内,再通过排泥管23排到池外,通过排泥管23的自动控制阀门实现,可通过远程控制,手动阀门在自动控制阀门需要检修时可用,浸没式膜组件9每隔一定周期还需要进行药洗,药洗是将次氯酸钠溶液通过药洗总管15注入浸没式膜出水支管分向各浸没式膜组件,药洗完毕后将池内水通过排泥管全部排掉。
控制柜33在完成上述控制过程的同时,实时监控,每个电动设备状态时刻记录在控制柜33中,出现异常及时控制预先配置的声光报警装置报警。 While completing the above control process, the control cabinet 33 monitors in real time, records the status of each electric device in the control cabinet 33 at all times, and controls the pre-configured sound and light alarm device to alarm in time when abnormalities occur. the
综上,本发明与传统工艺比较具有以下优点: In summary, the present invention has the following advantages compared with traditional techniques:
第一,气浮膜滤净化系统将气浮工艺和膜过滤工艺有机结合,气浮分离与膜过滤在同一个池子里完成,充分利用了气浮池分离区的空间,不用另外修建池子,节省占地面积及造价;以相同处理量的万吨水厂为例,若按传统气浮加砂滤池工艺设计,气浮出水接砂滤池,设计滤速7m/h,则净过滤面积需要60平方米,加上砂滤池前后进出水区及结构墙,需在气浮膜滤净化系统占地面积基础上至少增加约100平方米的面积用来修建滤池;若按传统气浮加超滤膜工艺 设计,采用外径160mm的超滤膜,单只产水量1t/h,则需要670根膜,将这些膜及配套管道布置下来,需在气浮膜滤净化系统占地面积基础上至少增加约200平方米的面积。 First, the air flotation membrane filtration purification system organically combines the air flotation process and the membrane filtration process, and the air flotation separation and membrane filtration are completed in the same pool, which makes full use of the space in the separation area of the air flotation pool, and does not need to build another pool, saving the occupied area. Land area and cost; taking a 10,000-ton water plant with the same treatment capacity as an example, if the traditional air flotation and sand filter process is designed, the air flotation outlet is connected to the sand filter, and the design filtration rate is 7m/h, the net filtration area needs 60 square meters, plus the water inlet and outlet areas and structural walls before and after the sand filter, it is necessary to add at least about 100 square meters of area to the construction of the filter on the basis of the area occupied by the air flotation membrane filtration purification system; The ultrafiltration membrane process design uses an ultrafiltration membrane with an outer diameter of 160mm, and a single water production rate of 1t/h requires 670 membranes. To arrange these membranes and supporting pipelines, the air flotation membrane filtration purification system needs to be based on the floor area. At least increase the area of about 200 square meters. the
第二,气浮膜滤净化系统将气浮分离作为膜过滤处理的预处理,能提高膜过滤处理的抗负荷能力,同时气浮产生的微气泡对浸没式膜组件的膜丝表面有摩擦清洗作用,能提高膜的抗污染性,而反过来膜过滤处理出水代替气浮传统的集水槽或穿孔管集水出水方式,又能大幅提高气浮处理的出水水质;气浮膜滤净化系统内膜组件过滤精度高,能保证最后出水浊度在0.2NTU以下,而砂滤池随过滤时间的增长,若反洗不及时,很容易存在滤池穿透现象,出水浊度无法保证在1NTU以下,气浮膜滤净化系统出水水质明显优于砂滤池。 Second, the air flotation membrane filtration purification system uses air flotation separation as the pretreatment of the membrane filtration treatment, which can improve the load resistance of the membrane filtration treatment, and at the same time, the microbubbles generated by the air flotation can frictionally clean the surface of the membrane filaments of the submerged membrane module The function can improve the anti-pollution of the membrane, and in turn, membrane filtration can replace the traditional water collection tank or perforated pipe water collection and discharge method of air flotation, and can greatly improve the effluent water quality of air flotation treatment; the air flotation membrane filtration purification system Membrane modules have high filtration precision and can ensure that the turbidity of the final effluent is below 0.2NTU. However, with the increase of the filtration time of the sand filter, if the backwashing is not timely, it is easy to have filter penetration, and the turbidity of the effluent cannot be guaranteed to be below 1NTU. , The effluent quality of the air flotation membrane filtration purification system is obviously better than that of the sand filter. the
第三,气浮膜滤净化系统在池子底部设置多个锥形泥斗,对池内膜组件进行反洗的过程中产生的污染物,经过重力静沉落入泥斗内,通过串联各泥斗的排泥管排向池外,不用将整个池子的水排掉,降低了水厂的自用水率;第四,气浮膜滤净化系统反冲洗周期短、时间短、用水量小。相同处理量的万吨水厂,气浮膜滤净化系统一次反冲洗时间是砂滤池的十分之一,消耗水量是砂滤池的七分之一,反冲洗周期比超滤膜反冲洗周期延长1倍以上。 Thirdly, the air flotation membrane filtration purification system sets multiple conical mud hoppers at the bottom of the pool. The mud discharge pipe of the bucket is discharged out of the pool, without draining the water of the entire pool, which reduces the self-water rate of the water plant; fourth, the backwash cycle of the air flotation membrane filtration purification system is short, the time is short, and the water consumption is small. For a 10,000-ton water plant with the same processing capacity, the backwashing time of the air flotation membrane filtration purification system is one-tenth of that of the sand filter, the water consumption is one-seventh of the sand filter, and the backwashing cycle is shorter than that of the ultrafiltration membrane. The period is more than doubled. the
第五,气浮膜滤净化系统膜组件安装简单,维修方便。相同处理量的万吨水厂,施工工期比超滤膜缩短5天左右,安装材料比超滤膜减少20%。 Fifth, the membrane components of the air flotation membrane filtration purification system are easy to install and easy to maintain. For a 10,000-ton water plant with the same treatment capacity, the construction period is about 5 days shorter than that of ultrafiltration membranes, and the installation materials are 20% less than that of ultrafiltration membranes. the
第六,气浮膜滤净化系统只需要一台泵即可实现产水与反洗功能,而超滤膜需要两台泵来实现。 Sixth, the air flotation membrane filtration purification system only needs one pump to realize the functions of water production and backwashing, while the ultrafiltration membrane needs two pumps to realize it. the
第七,气浮膜滤净化系统控制装置自动完成气浮膜滤净化系统的工艺自动操作,大大减少了人为操作,提高了劳动生产力。 Seventh, the control device of the air flotation membrane filtration purification system automatically completes the process automatic operation of the air flotation membrane filtration purification system, which greatly reduces human operations and improves labor productivity. the
以上所述,仅是本发明的较佳实施例而已,并非对本发明作任何形式上的限制,虽然本发明已以较佳实施例揭露如上,然而并非用以限定本发明,任何熟悉本专业的技术人员在不脱离本发明技术方案范围内,当可利用上诉揭示的技术内容做出些许更动或修饰为等同变化的等效实施例,但凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施例所做的任何简单修改、等同变化与修饰,均仍属于本发明技术方案的范围内。 The above description is only a preferred embodiment of the present invention, and does not limit the present invention in any form. Although the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone familiar with this field Without departing from the scope of the technical solution of the present invention, the skilled person can use the technical content disclosed in the appeal to make some changes or modify it into an equivalent embodiment with equivalent changes, but any content that does not depart from the technical solution of the present invention, according to the present invention Any simple modifications, equivalent changes and modifications made to the above embodiments still fall within the scope of the technical solutions of the present invention. the
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