CN206473882U - 一种串联式多级过滤装置 - Google Patents
一种串联式多级过滤装置 Download PDFInfo
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- CN206473882U CN206473882U CN201621179684.7U CN201621179684U CN206473882U CN 206473882 U CN206473882 U CN 206473882U CN 201621179684 U CN201621179684 U CN 201621179684U CN 206473882 U CN206473882 U CN 206473882U
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- filter
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- 238000010521 absorption reaction Methods 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical group 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Abstract
本实用新型公开了一种串联式多级过滤装置,包括多个过滤单元,过滤单元包括过滤器主体以及进水口、出水口、滤料层、承托层,在过滤器主体底部设有反冲洗进水管,在进水口与滤料层之间设有反冲洗出水渠;出水口和反冲洗进水管上设有阀门,以控制出水口和反冲洗进水管的开闭;所述过滤单元之间依次连接组成多级串联;单个过滤单元中只包含单层滤料。本实用新型将过滤单元多级串联,有效防止了多层滤料之间的混杂,方便滤料更换,使滤料的选择更自由;过滤单元中滤料粒径逐级递减,有效减小滤池的水头损失,提高过滤效果;不同级中滤料可以分别单独冲洗,更易控制反冲洗参数,减少了反冲洗的能耗;溢流出水口能排出多余的水以防止过滤器受损。
Description
一种串联式多级过滤装置
技术领域
[0001] 本实用新型属于水处理技术领域,具体涉及一种串联式多级过滤装置。
背景技术
[0002] 过滤作为水处理中非常重要的环节,是保证出水水质浊度达标的重要措施。过滤 的功效,不仅仅在于进一步降低水的浊度,还应该随着浊度的降低部分去除水中的有机物、 细菌乃至病毒等。根据滤料层的层数不同,分为单层均质滤料、双层滤料、三层滤料和混合 滤料。三层滤料占据平均粒径由上而下递减的优点,使得其不仅含污能力大,且因下层重质 滤料粒径很小,对保证滤后水质有很大作用。但三层滤料存在缺陷,即反冲洗时易发生混层 现象,降低了滤料的有效使用期,且难以控制反冲洗参数,反冲洗能耗大。
[0003] 滤料及滤料层的构成是过滤技术中重要组成部分,是决定过滤设备性能优劣的关 键,决定着滤后水水质与过滤设备的基本性能,因此过滤技术的发展在很大程度上取决于 对滤料和滤料层构成的研究与改进。例如中国专利号为200980126068.1,发明创造名称为 “多级水过滤器”;专利号为200910154854.4,发明创造名称为“多级过滤滤芯”和专利号为 201310427555.X,发明创造名称为“一种多级渗透过滤净化装置”等先后公开了不同结构的 多级过滤反应装置。前两者为过滤器或净水器中的过滤构件,核心滤料为活性炭滤料或纤 维复合材料,结构简单,占用体积小,适用于家用小型净水器。后者虽然是多级过滤反应装 置,但与本反应装置在结构上大有不同,其滤料在同一个过滤反应器内,类似于多层过滤, 虽然每层有滤网将滤料隔开,但滤网易堵塞,水头损失会相应的增加,过滤周期会相应缩 短,且位置偏下层的滤料更新较为麻烦。 实用新型内容
[0004] 针对现有技术所存在的不足,本实用新型所解决的问题在于,怎样提供一种滤料 不会混杂、反冲洗效率高能耗小、滤料更换方便、过滤效果更好的串联式多级过滤装置。
[0005] 为实现上述目的,本实用新型采用如下方案:
[0006] —种串联式多级过滤装置,其特征在于:包括多个过滤单元,所述过滤单元包括过 滤器主体以及设在主体上部的进水口、设在主体底部的出水口、设在主体中部的滤料层、设 在滤料层与出水口之间的承托层,所述过滤器主体在底部还设有反冲洗进水管,在进水口 与滤料层之间设有可开闭的反冲洗出水渠;反冲洗进水管一端接出水口,另一端与反冲洗 栗连接;在反冲洗进水管靠近出水口的位置设有出水管,所述出水管和反冲洗进水管上设 有阀门,以控制出水管和反冲洗进水管的开闭;所述过滤单元之间通过上一级过滤单元的 出水管与下一级过滤单元的进水口相连接的方式依次组成多级串联;单个过滤单元中只包 含单层滤料。
[0007] 作为进一步优化,沿着过滤水流经过的顺序,所述多级过滤单元中滤料的粒径从 大到小依次递减。
[0008]作为进一步优化,所述过滤单元有三级,第一级中滤料为粒径0.8-1.6mm的无烟煤 滤料,第二级中滤料为粒径0.5-0.8mm的沸石或石英砂滤料,第三级中滤料为粒径0.25-0.5mm的瓷砂或重质矿石滤料。
[0009] 作为进一步优化,所述进水口还包括进水口布水渠。
[0010] 作为进一步优化,所述过滤单元在进水口与反冲洗出水渠之间设有溢流出水口。
[0011] 作为进一步优化,所述溢流出水口设置在靠近进水口的位置。
[0012] 作为进一步优化,所述承托层包括承托板,承托板上放置大粒径的鹅卵石,粒径范 围为 2_16mm。
[0013] 作为进一步优化,所述反冲洗出水渠的高度不小于滤料完全膨胀时的高度。
[0014] 作为进一步优化,每一级过滤单元的出水管水平延伸绕开过滤器主体后向上弯 折,弯折到一定高度后再水平弯折并与下一级过滤单元的进水口连接,弯折高度位于该级 滤料层高度之间;最后一级过滤单元的出水管水平弯折后再竖直向下弯折,弯折到出水管 与反冲洗进水管连接位置后水平弯折。
[0015] 作为进一步优化,所有过滤单元反冲洗进水管通过同一主管道与共同的反冲洗栗 连接。
[0016] 相比于现有技术,本实用新型具有如下有益效果:
[0017] 1、本实用新型采用将过滤单元多级串联,每个过滤单元只设置一种滤料,有效地 防止了多层滤料之间的混杂,解除了对滤料层数的限制,方便滤料的更换,使滤料的选择更 自由;
[0018] 2、本实用新型过滤单元中滤料的粒径从大到小逐级递减,可以有效减小滤池的水 头损失,延长过滤周期,提高过滤效果,还可以减少混凝过程药剂投加量,缩短沉淀时间,甚 至于取消混凝沉淀工艺;
[0019] 3、本实用新型中不同级中的滤料可以通过阀门控制分别单独冲洗,使得反冲洗参 数控制更容易,减少了反冲洗的能耗,效率高,连接到同一个反冲洗栗还方便统一反冲洗;
[0020] 4、本实用新型在在进水口与反冲洗出水渠之间设置了溢流出水口,能排出多余的 水以防止过滤器受损,可起到一定的保护作用;
[0021] 5、本实用新型的出水管设置成连续弯折的形状,可以抬高出水高度,能有效避免 过滤单位内部出现负水头现象,从而减轻滤层气阻。
附图说明
[0022] 图1为本实用新型过滤单元结构示意图;
[0023] 图2为本实用新型串联式多级过滤装置示意图;
[0024] 图中,1-过滤器主体,2-进水口,3-出水管,4-滤料层,5-承托层,51-承托板,6-反 冲洗进水管,7-反冲洗出水渠,8-溢流出水口,9-反冲洗栗,10-阀门。
具体实施方式
[0025] 下面结合附图对本实用新型作进一步详细描述,但本实用新型的实施方式不限于 此。
[0026] 实施例:
[0027] —种串联式多级过滤装置,如图1-2所示,包括多个过滤单元,所述过滤单元包括 过滤器主体1以及设在主体1上部的进水口 2、设在主体1底部的出水口、设在主体1中部的滤 料层4、设在滤料层4与出水口之间的承托层5,所述过滤器主体1在底部还设有反冲洗进水 管6,在进水口 2与滤料层4之间设有可开闭的反冲洗出水渠7;反冲洗进水管6—端接出水 口,另一端与反冲洗栗连接;在反冲洗进水管6靠近出水口的位置设有出水管3,所述出水管 3和反冲洗进水管6上设有阀门10,以控制出水管3和反冲洗进水管6的开闭;所述过滤单元 之间通过一过滤单元的出水口 3与另一过滤单元的进水口 2相连接的方式依次组成多级串 联;单个过滤单元中只包含单层滤料。
[0028] 当对进水进行过滤时,关闭全部的反冲洗进水管和反冲洗出水渠,打开全部出水 口;此时进水从第一级过滤单元的进水口进入,经过多级过滤后从最后一级过滤单元的出 水口流出。经过一段时间的过滤,滤料上附着的污染物逐渐增加,使滤层的阻力逐渐变大, 水头损失也随之增大,当达到最大允许水头损失时,需停止过滤对滤料进行反冲洗。当对滤 料进行反冲洗时,关闭所有出水口,打开某一级过滤单元的反冲洗进水管和反冲洗出水渠; 此时反冲洗栗抽水进行反冲洗,冲洗水通过反冲洗进水管进入过滤器主体,将过滤层中的 污染物冲刷出来后由反冲洗出水渠流出。如此即可实现对该级滤料的反冲洗,若要全部反 冲洗则打开所有过滤单元的反冲洗进水管和反冲洗出水渠。
[0029] 串联式多级过滤装置有很多优点:一,虽然理论上滤料的层数越多越好,但由于在 实际应用中,传统多层滤料中存在很多问题,比如相邻两层滤料间易混杂、滤料易流失、加 工复杂等,对滤料层数就有了限制,导致生产中所采用的仍然是双层或三层的滤料,难以继 续增加;而本实用新型中的串联式多级过滤装置,通过每级过滤单元只包含一种滤料,并将 其多级串联组合,不但解决了多层滤料存在的上述问题,还打破了对滤料层数的限制,串联 的级数可以根据需求任意增加。二,传统多层滤料在反冲洗时不仅易发生混层,降低了滤料 的有效使用期,还难以控制反冲洗参数,反冲洗能耗大;而本实用新型中的串联式多级过滤 装置可通过阀门的开闭实现每一级过滤单元的单独反冲洗,反冲洗参数更易控制,能耗减 小效果显著,效率更高。三,本实用新型中的串联式多级过滤装置还能充分利用不同滤料对 不同污染物去除效果的互补作用,根据实际情况更换所需的滤料,满足有效去除多种污染 物的要求,由于采用多级结构,其对滤料的更换比传统多层滤料结构更加方便快捷,根据需 要还能很容易地调整级与级之间的过滤顺序。四,传统多层滤料还要考虑粒径和密度的要 求,以传统的三层滤料为例,三层滤料之间需满足“粒径:上层> 中层 >下层”以及“密度:上 层< 中层<下层”的条件,才能保证滤料不易混层,达到较好的过滤效果,这样一来就对滤 料的选择有了一定的限制;而本实用新型中的串联式多级过滤装置并不需要满足上述对滤 料密度的要求,这样一来对滤料的选择就变得更加自由,只需考虑滤料的过滤效果,有利于 找出比传统多层滤料过滤效果更好的滤料组合。
[0030] 沿着过滤水流经过的顺序,所述多级过滤单元中滤料的粒径从大到小依次递减。 由大到小的滤料级联组合不仅可以减小滤池的水头损失,延长过滤周期,提高过滤效果,还 可以减少混凝过程药剂投加量,缩短沉淀时间,甚至可以取消混凝沉淀工艺,直接应用在村 镇地区的水处理厂站。
[0031] 以三级过滤装置为例,从第一级到第三级,依次为:大颗粒过滤单元,放置大粒径 滤料;中颗粒过滤单元,放置中粒径滤料;小颗粒过滤单元,放置小粒径滤料。其中,大粒径 滤料可以为粒径0.8-1.6mm的无烟煤滤料,中粒径滤料可以为粒径0.5-0.8mm的沸石或石英 砂滤料,小粒径滤料可以为粒径0.25-0.5mm的瓷砂或重质矿石滤料。进水首先经过大颗粒 过滤单元发生截留、筛滤、粘附以及吸附作用,然后流过中颗粒过滤单元进一步截留吸附, 最后经过小颗粒过滤单元进行深度过滤。进水口上可安装一个流量计调整进水流量以调节 滤速,过滤后的水通过出水口输送到下一步的工艺流程中。
[0032] 所述进水口 2还包括进水口布水渠。进水口设置布水渠可以让进水较为均匀地流 向滤料。
[0033] 所述过滤单元在进水口 2与反冲洗出水渠7之间设有溢流出水口 8。若过滤层中堆 积了过多的污染物造成过滤层发生堵塞,导致过滤器主体内的压力过大,此时进水口下方 的溢流出水口可以排出多余的水以防止过滤器受损,起到一定的保护作用。
[0034] 所述溢流出水口 8设置在靠近进水口 2的位置。这样可以在实际使用中方便操作。
[0035] 所述承托层5包括承托板51,承托板51上放置大粒径的鹅卵石,粒径范围为2-16_。这样可以防止滤料从集水系统中流失,在反冲洗时可起到均匀布水铺助作用。
[0036] 每一级过滤单元的出水管3水平延伸绕开过滤器主体1后向上弯折,弯折到一定高 度后再水平弯折并与下一级过滤单元的进水口 2连接,弯折高度位于该级滤料层4高度之 间;最后一级过滤单元的出水管3水平弯折后再竖直向下弯折,弯折到出水管3与反冲洗进 水管6连接位置后水平弯折。这样一来可以抬高出水高度,能有效避免过滤单位内部出现负 水头现象,从而减轻滤层气阻。
[0037] 所有过滤单元反冲洗进水管6通过同一主管道与共同的反冲洗栗9连接。这样可以 更方便统一对过滤单元进行反冲洗。
[0038] 所述反冲洗出水渠7的高度不小于滤料完全膨胀时的高度。也就是说反冲洗出水 渠与承托层之间的距离多滤料厚度X (1+滤料反冲洗膨胀率),这样在反冲洗时,可以保证 滤料不会从反冲洗出水渠流出过滤器导致滤料的流失。
[0039] 举例说明过滤单元的尺寸及内部的安装位置,作为优选,设过滤器主体总高h = Im,从下至上依次有:承托板与底部的距离= 0.05h = 5cm、承托层高度=0. Ih= 10cm、滤料 厚度= 〇.4h = 40cm,若反冲洗膨胀率25%,则反冲洗出水渠与滤料表层之间为IOcm (即反冲 洗出水渠与承托层距离50cm),溢流口距反冲洗出水渠=0.2h = 20cm,池顶超出溢流口 15cm〇
[0040] 过滤单元横断面面积为:
[0042] 过滤单元长宽比取1:1,则每个过滤单元为正方体结构。
[0043] 其中,Q—设计水量(m3/d);
[0044] V一设计滤速,取8〜10m/h;
[0045] T一每日实际工作时间,一般取24h。
[0046] 最后说明的是,以上实施例仅用以说明本实用新型的技术方案而非限制,尽管参 照较佳实施例对本实用新型进行了详细说明,本领域的普通技术人员应当理解,可以对本 实用新型的技术方案进行修改或者等同替换,而不脱离本实用新型技术方案的宗旨和范 围,其均应涵盖在本实用新型的权利要求范围当中。
Claims (10)
1. 一种串联式多级过滤装置,其特征在于:包括多个过滤单元,所述过滤单元包括过滤 器主体以及设在主体上部的进水口、设在主体底部的出水口、设在主体中部的滤料层、设在 滤料层与出水口之间的承托层,所述过滤器主体在底部还设有反冲洗进水管,在进水口与 滤料层之间设有可开闭的反冲洗出水渠;反冲洗进水管一端接出水口,另一端与反冲洗栗 连接;在反冲洗进水管靠近出水口的位置设有出水管,所述出水管和反冲洗进水管上设有 阀门,以控制出水管和反冲洗进水管的开闭;所述过滤单元之间通过上一级过滤单元的出 水管与下一级过滤单元的进水口相连接的方式依次组成多级串联;单个过滤单元中只包含 单层滤料。
2. 根据权利要求1所述的串联式多级过滤装置,其特征在于:沿着过滤水流经过的顺 序,所述多级过滤单元中滤料的粒径从大到小依次递减。
3. 根据权利要求2所述的串联式多级过滤装置,其特征在于:所述过滤单元有三级,第 一级中滤料为粒径〇. 8-1.6mm的无烟煤滤料,第二级中滤料为粒径0.5-0.8mm的沸石或石英 砂滤料,第三级中滤料为粒径〇. 25-0.5_的瓷砂或重质矿石滤料。
4. 根据权利要求1所述的串联式多级过滤装置,其特征在于:所述进水口还包括进水口 布水渠。
5. 根据权利要求1所述的串联式多级过滤装置,其特征在于:所述过滤单元在进水口与 反冲洗出水渠之间设有溢流出水口。
6. 根据权利要求5所述的串联式多级过滤装置,其特征在于:所述溢流出水口设置在靠 近进水口的位置。
7. 根据权利要求1所述的串联式多级过滤装置,其特征在于:所述承托层包括承托板, 承托板上放置大粒径的鹅卵石,粒径范围为2-16mm。
8. 根据权利要求1所述的串联式多级过滤装置,其特征在于:所述反冲洗出水渠的高度 不小于滤料完全膨胀时的高度。
9. 根据权利要求1所述的串联式多级过滤装置,其特征在于:每一级过滤单元的出水管 水平延伸绕开过滤器主体后向上弯折,弯折到一定高度后再水平弯折并与下一级过滤单元 的进水口连接,弯折高度位于该级滤料层高度之间;最后一级过滤单元的出水管水平弯折 后再竖直向下弯折,弯折到出水管与反冲洗进水管连接位置后水平弯折。
10. 根据权利要求1所述的串联式多级过滤装置,其特征在于:所有过滤单元反冲洗进 水管通过同一主管道与共同的反冲洗栗连接。
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CN106310746A (zh) * | 2016-10-27 | 2017-01-11 | 重庆大学 | 串联式多级过滤装置 |
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