CN107445340A - 一种活性炭滤池反冲洗水回收装置及回收方法 - Google Patents
一种活性炭滤池反冲洗水回收装置及回收方法 Download PDFInfo
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- CN107445340A CN107445340A CN201710740584.XA CN201710740584A CN107445340A CN 107445340 A CN107445340 A CN 107445340A CN 201710740584 A CN201710740584 A CN 201710740584A CN 107445340 A CN107445340 A CN 107445340A
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- water
- activated carbon
- backwashing water
- carbon filter
- backwashing
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 170
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound data:image/svg+xml;base64,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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 121
- 238000011001 backwashing Methods 0.000 title claims abstract description 92
- 238000011084 recovery Methods 0.000 title claims abstract description 15
- 239000012528 membrane Substances 0.000 claims abstract description 60
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound 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[O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 44
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 42
- 238000006385 ozonation reaction Methods 0.000 claims abstract description 19
- 238000005189 flocculation Methods 0.000 claims description 13
- 230000016615 flocculation Effects 0.000 claims description 13
- 230000003647 oxidation Effects 0.000 claims description 12
- 238000007254 oxidation reaction Methods 0.000 claims description 12
- 238000001556 precipitation Methods 0.000 claims description 10
- 239000006228 supernatant Substances 0.000 claims description 10
- 238000010907 mechanical stirring Methods 0.000 claims description 7
- 238000007599 discharging Methods 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 239000000084 colloidal system Substances 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 230000003334 potential Effects 0.000 claims description 3
- 238000005273 aeration Methods 0.000 claims description 2
- 238000009298 carbon filtering Methods 0.000 claims description 2
- 230000000694 effects Effects 0.000 claims description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K Aluminium chloride Chemical compound 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Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims 2
- 239000007789 gas Substances 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
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- 238000005259 measurement Methods 0.000 description 1
- NPDODHDPVPPRDJ-UHFFFAOYSA-N permanganate Chemical compound 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[O-][Mn](=O)(=O)=O NPDODHDPVPPRDJ-UHFFFAOYSA-N 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 230000001376 precipitating Effects 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000005429 turbidity Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water, or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
Abstract
本发明公开了一种活性炭滤池反冲洗水回收装置及回收方法，包括絮凝剂投加池、反冲洗水收集池、超滤膜池、臭氧发生器和清水池；反冲洗水收集池上设置有反冲洗水入口、絮凝剂投加口和收集池出水口；超滤膜池内设置有超滤膜组件，超滤膜组件顶部设置有超滤膜出水口和超滤膜反冲洗入水口；超滤膜出水口与清水池的入水口相连接；清水池上设置有反冲洗出水口，该反冲洗出水口通过反冲洗泵与超滤膜反冲洗入水口相连接；超滤膜池内设有臭氧曝气盘。本发明能将活性炭滤池反冲洗水中的微生物、有机物以及颗粒物进行滤除，实现了活性炭滤池反冲洗水的安全利用，提高了给水厂节水效率，并且可在低药耗的前提下有效抑制超滤膜污染。
Description
一种活性炭滤池反冲洗水回收装置及回收方法
技术领域
[0001] 本发明涉及给水厂生产废水处理领域，特别是一种活性炭滤池反冲洗水回收装置 及回收方法。
背景技术
[0002] 作为供水企业和社会节水的重要组成部分，水厂节水尤其是排泥水再利用已成为 业内节水技术发展的必然趋势。据调查，全国地表水厂拥有生产废水处理设施的不足5%，即 绝大部分水厂的生产废水均未经处理直接排放，不仅浪费严重，而且对受纳水体也造成了 较为严重的污染。
[0003] 近年来，以臭氧-生物活性炭为代表的深度处理工艺在全国得到逐渐的推广和应 用，活性炭滤池反冲洗水量约占水厂日供水量的2%。以南京为例，日供水能力达200万m3，按 水厂生产废水量5%〜8%进行估算，生产废水量达10〜16万m3/d，相当于一座50万人口左右中 等城市的用水量，节水潜力可观。
[0004] 目前活性炭滤池反冲洗水的再利用主要是将反冲洗水回用至与原水混合，这种回 用方式优点是方式简单，减少回收利用成本。然而，活性炭滤池反冲洗水中含有大量的微生 物、有机物以及反冲洗过程中被冲起的颗粒物。这种反冲洗水回用与原水混合后可能会导 致混凝出水中溶解性有机物含量增加以及微生物泄露等问题，对水厂供水安全性有着一定 的风险。
发明内容
[0005] 本发明要解决的技术问题是针对上述现有技术的不足，而提供一种活性炭滤池反 冲洗水回收装置，该活性炭滤池反冲洗水回收装置能将活性炭滤池反冲洗水中的微生物、 有机物以及颗粒物进行滤除，实现了活性炭滤池反冲洗水的安全利用，提高了给水厂节水 效率，并且可在低药耗的前提下有效抑制超滤膜污染。
[0006] 为解决上述技术问题，本发明采用的技术方案是： 一种活性炭滤池反冲洗水回收装置，包括絮凝剂投加池、反冲洗水收集池、超滤膜池、 臭氧发生器和清水池。
[0007] 絮凝剂投加池内装填有絮凝剂。
[0008] 反冲洗水收集池上设置有反冲洗水入口、絮凝剂投加口和收集池出水口；其中，反 冲洗水入口与活性炭滤池反冲洗水相连接，絮凝剂投加口通过絮凝剂管路与絮凝剂投加池 的出口相连接，收集池出水口与超滤膜池的入水口相连接。
[0009] 超滤膜池内设置有超滤膜组件，超滤膜组件顶部设置有超滤膜出水口和超滤膜反 冲洗入水口；其中，超滤膜出水口与清水池的入水口相连接。
[0010] 清水池上设置有反冲洗出水口，该反冲洗出水口通过反冲洗栗与超滤膜反冲洗入 水口相连接。
[0011] 位于超滤膜组件下方的超滤膜池内还设置有臭氧曝气盘，臭氧曝气盘通过管路与 臭氧发生器相连接。
[0012] 超滤膜池顶部还设置有臭氧尾气排出口。
[0013] 反冲洗水收集池内设置有机械搅拌装置，反冲洗水收集池底部设置有机械刮泥机 和排泥口。
[0014] 絮凝剂管路上设置有计量栗和阀门。
[0015] 臭氧发生器与臭氧曝气盘相连接的管路上设置有流量计。
[0016] 本发明还提供一种活性炭滤池反冲洗水回收方法，该活性炭滤池反冲洗水回收方 法能将活性炭滤池反冲洗水中的微生物、有机物以及颗粒物进行滤除，实现了活性炭滤池 反冲洗水的安全利用，提高了给水厂节水效率，并且可在低药耗的前提下有效抑制超滤膜 污染。
[0017] —种活性炭滤池反冲洗水回收方法，包括如下步骤。
[0018] 步骤1，收集活性炭滤池反冲洗水。
[0019] 步骤2,将步骤1收集的活性炭滤池反冲洗水进行微絮凝处理。
[0020] 步骤3，将步骤2微絮凝后的活性炭滤池反冲洗水进行沉淀。
[0021] 步骤4,将步骤3沉淀后的上清液进行臭氧预氧化后进入超滤膜组件进行超滤。
[0022] 步骤5，将步骤4中的超滤膜出水进入清水池回用。
[0023] 步骤1中，收集的活性炭滤池反冲洗水是指活性炭滤池反冲洗开始Imin后的反冲 洗水。
[0024] 步骤2中的微絮凝及步骤3中的沉淀均在反冲洗水收集池中进行，反冲洗水收集池 中设机械搅拌装置，活性炭滤池反冲洗水收集结束后，投加絮凝剂并进行搅拌;然后，静置 沉淀。
[0025] 所述絮凝剂为聚合氯化铝，投加量2〜10 mg/L，絮凝剂投加及搅拌完毕后，应使絮 凝后的活性炭滤池反冲洗水的zeta电位为-0.15〜0.15mV;絮凝剂投加后的搅拌时间为0.5-2 min，絮凝后的静置时间不少于30min。
[0026] 步骤4中，臭氧预氧化与超滤膜超滤均在超滤膜池中进行，臭氧曝气盘设置在超滤 膜池的底部，超滤膜组件设置在臭氧曝气盘上方的超滤膜池中，臭氧曝气盘与臭氧发生器 相连接。
[0027] 臭氧预氧化时，臭氧与步骤3沉淀后的上清液的接触时间不少于10 min，臭氧投加 量需满足要求为:臭氧与沉淀后上清液接触10 min后，采用静滴法，测得超滤膜池中的胶体 与纯水的接触角小于60°。
[0028] 本发明具有的有益效果是：能将活性炭滤池反冲洗水中的微生物、有机物以及颗 粒物进行滤除，实现了活性炭滤池反冲洗水的安全利用，提高了给水厂节水效率，并且可在 低药耗的前提下有效抑制超滤膜污染。
附图说明
[0029] 图1显示了本发明一种活性炭滤池反冲洗水回收装置的结构示意图。
[0030] 图2显示了超滤膜组件在有预氧化和无预氧化运行时跨膜压差对比图。
[0031] 其中有： 10.絮凝剂投加池；11.计量栗；12.阀门； 20.反冲洗水收集池;21.反冲洗水入口； 22.絮凝剂投加口； 23.机械搅拌装置;24.机械 刮泥机;25.排泥口； 26.离心栗;27.收集池出水口； 30.超滤膜池;31.超滤膜组件;311.超滤膜出水口； 312.超滤膜反冲洗入水口； 32.臭氧 曝气盘;33.臭氧尾气排出口； 40.臭氧发生器;41.流量计;50.清水池;51.压力计;52.产水栗;53.反冲洗栗;54.反冲 洗出水口； 60.臭氧破坏装置。
具体实施方式
[0032] 下面结合附图和具体较佳实施方式对本发明作进一步详细的说明。
[0033] 如图1所示，一种活性炭滤池反冲洗水回收装置，包括絮凝剂投加池10、反冲洗水 收集池20、超滤膜池30、臭氧发生器40和清水池50。
[0034] 絮凝剂投加池内装填有絮凝剂。
[0035] 反冲洗水收集池20上设置有反冲洗水入口 21、絮凝剂投加口 22和收集池出水口 27〇
[0036] 反冲洗水入口与活性炭滤池反冲洗水相连接。
[0037] 絮凝剂投加口通过絮凝剂管路与絮凝剂投加池的出口相连接，絮凝剂管路上优选 设置有计量栗11和阀门12。
[0038] 收集池出水口优选通过离心栗26和阀门与超滤膜池的入水口相连接。
[0039] 另外，上述反冲洗水收集池内还优选设置有机械搅拌装置23，活性炭滤池反冲洗 水收集结束后，投加絮凝剂时用于搅拌。
[0040] 进一步，反冲洗水收集池底部优选设置有机械刮泥机24和排泥口 25，用于定期排 放反冲洗水收集池内的沉淀污泥。
[0041] 超滤膜池30内设置有超滤膜组件31，超滤膜组件顶部设置有超滤膜出水口 311和 超滤膜反冲洗入水口 312。
[0042] 超滤膜出水口优选通过阀门、压力计51和产水栗52与清水池的入水口相连接。
[0043] 清水池50上设置有反冲洗出水口 54,该反冲洗出水口通过反冲洗栗53与超滤膜反 冲洗入水口相连接。
[0044]位于超滤膜组件下方的超滤膜池内还设置有臭氧曝气盘32,臭氧曝气盘通过管路 与臭氧发生器40相连接;臭氧发生器与臭氧曝气盘相连接的管路上优选设置有流量计41。
[0045] 超滤膜池顶部还优选设置有臭氧尾气排出口 33，与臭氧尾气排出口 33相连接的排 气管路上优选设置有臭氧破坏装置60。
[0046] —种活性炭滤池反冲洗水回收方法，包括如下步骤。
[0047] 步骤1，收集活性炭滤池反冲洗水。
[0048] 由于活性炭滤池在反冲洗初期的活性炭滤池反冲洗水中含有大量的杂质与微生 物，为减轻回收系统负担，同时考虑回用水质安全性，反冲洗开始后I min内的反冲洗水不 收集，I min后，收集活性炭滤池反冲洗水，移入收集容器中。因此，本步骤1中，收集的活性 炭滤池反冲洗水是指活性炭滤池反冲洗开始Imin后的反冲洗水。
[0049] 步骤2,将步骤1收集的活性炭滤池反冲洗水进行微絮凝处理。
[0050] 步骤3，将步骤2微絮凝后的活性炭滤池反冲洗水进行沉淀。
[0051] 上述步骤2中的微絮凝及步骤3中的沉淀均在反冲洗水收集池中进行，反冲洗水收 集池中设机械搅拌装置，活性炭滤池反冲洗水收集结束后，投加絮凝剂并进行搅拌;然后， 静置沉淀。
[0052] 投加的絮凝剂优选为聚合氯化铝，投加量优选为2〜10 mg/L，絮凝剂投加量的依据 为：絮凝剂投加及搅拌完毕后，应使絮凝后的活性炭滤池反冲洗水的zeta电位为-0.15〜 0.15mV〇 另外，絮凝剂投加后的搅拌时间优选为0.5-2 min，进一步优选为2min，絮凝后的静置 时间不少于30min，优选为30min。
[0053] 步骤4,将步骤3沉淀后的上清液进行臭氧预氧化后进入超滤膜组件进行超滤。
[0054] 沉淀结束后，取反冲洗水收集池中的上清液进入超滤膜池。本试验中超滤膜组件 采用PVC中空纤维膜，切割分子量为50000 Da，膜孔径0.01 μπι。
[0055] 臭氧预氧化与超滤膜超滤均在超滤膜池中进行，臭氧曝气盘设置在超滤膜池的底 部，超滤膜组件设置在臭氧曝气盘上方的超滤膜池中，臭氧曝气盘与臭氧发生器相连接。制 备的臭氧通过臭氧曝气盘进入水中，臭氧投加量I mg/L。
[0056] 臭氧预氧化时，臭氧与步骤3沉淀后的上清液的接触时间不少于10 min，臭氧投加 量需满足要求为:臭氧与沉淀后上清液接触10 min后，采用静滴法，测得超滤膜池中的胶体 与纯水的接触角小于60°。
[0057] 本发明中，臭氧接触10 min后，采用静滴法(sessile drop method)测量水中的胶 体与纯水的接触角，接触角实测为57.3°。
[0058] 超滤膜组件中的超滤膜每I h进行一次反冲洗，反冲洗水采用膜池产水，也即清水 池中的水。
[0059] 当运行跨膜压差达到60 KPa进行化学清洗，化学清洗采用次氯酸钠溶液。超滤膜 运行跨膜压差见图2,由图2可以看出，臭氧预氧化可以显著降低膜污染，延长化学清洗周 期。
[0060] 步骤5，将步骤4中的超滤膜出水进入清水池回用。
[0061] 本实施例回用前后的水质数据见表1。
[0062] 表1
从表1可以看出，本实施方式药耗低、处理效率高，且出水水质优良，可以直接进入清水 池实现回用。
[0063] 以上详细描述了本发明的优选实施方式，但是，本发明并不限于上述实施方式中 的具体细节，在本发明的技术构思范围内，可以对本发明的技术方案进行多种等同变换，这 些等同变换均属于本发明的保护范围。
Claims (10)
1. 一种活性炭滤池反冲洗水回收装置，其特征在于:包括絮凝剂投加池、反冲洗水收集 池、超滤膜池、臭氧发生器和清水池； 絮凝剂投加池内装填有絮凝剂； 反冲洗水收集池上设置有反冲洗水入口、絮凝剂投加口和收集池出水口；其中，反冲洗 水入口与活性炭滤池反冲洗水排水管相连接，絮凝剂投加口通过絮凝剂管路与絮凝剂投加 池的出口相连接，收集池出水口与超滤膜池的入水口相连接； 超滤膜池内设置有超滤膜组件，超滤膜组件顶部设置有超滤膜出水口和超滤膜反冲洗 入水口；其中，超滤膜出水口与清水池的入水口相连接； 清水池上设置有反冲洗出水口，该反冲洗出水口通过反冲洗栗与超滤膜反冲洗入水口 相连接； 位于超滤膜组件下方的超滤膜池内还设置有臭氧曝气盘，臭氧曝气盘通过管路与臭氧 发生器相连接； 超滤膜池顶部还设置有臭氧尾气排出口。
2. 根据权利要求1所述的活性炭滤池反冲洗水回收装置，其特征在于:反冲洗水收集池 内设置有机械搅拌装置，反冲洗水收集池底部设置有机械刮泥机和排泥口。
3. 根据权利要求1所述的活性炭滤池反冲洗水回收装置，其特征在于：絮凝剂管路上设 置有计量栗和阀门。
4. 根据权利要求1所述的活性炭滤池反冲洗水回收装置，其特征在于:臭氧发生器与臭 氧曝气盘相连接的管路上设置有流量计。
5. —种活性炭滤池反冲洗水回收方法，其特征在于:包括如下步骤： 步骤1，收集活性炭滤池反冲洗水； 步骤2,将步骤1收集的活性炭滤池反冲洗水进行微絮凝处理； 步骤3，将步骤2微絮凝后的活性炭滤池反冲洗水进行沉淀； 步骤4，将步骤3沉淀后的上清液进行臭氧预氧化后进入超滤膜组件进行超滤； 步骤5，将步骤4中的超滤膜出水进入清水池回用。
6. 根据权利要求5所述的活性炭滤池反冲洗水回收方法，其特征在于:步骤1中，收集的 活性炭滤池反冲洗水是指活性炭滤池反冲洗开始Imin后的反冲洗水。
7. 根据权利要求5所述的活性炭滤池反冲洗水回收方法，其特征在于:步骤2中的微絮 凝及步骤3中的沉淀均在反冲洗水收集池中进行，反冲洗水收集池中设机械搅拌装置，活性 炭滤池反冲洗水收集结束后，投加絮凝剂并进行搅拌;然后，静置沉淀。
8. 根据权利要求7所述的活性炭滤池反冲洗水回收方法，其特征在于:所述絮凝剂为聚 合氯化铝，投加量2〜10 mg/L，絮凝剂投加及搅拌完毕后，应使絮凝后的活性炭滤池反冲洗 水的zeta电位为-0.15〜0.15mV;絮凝剂投加后的搅拌时间为0.5〜2 min，絮凝后的静置时间 不少于30min。
9. 根据权利要求5所述的活性炭滤池反冲洗水回收方法，其特征在于:步骤4中，臭氧预 氧化与超滤膜超滤均在超滤膜池中进行，臭氧曝气盘设置在超滤膜池的底部，超滤膜组件 设置在臭氧曝气盘上方的超滤膜池中，臭氧曝气盘与臭氧发生器相连接。
10. 根据权利要求9所述的活性炭滤池反冲洗水回收方法，其特征在于:臭氧预氧化时， 臭氧与步骤3沉淀后上清液的接触时间不少于10 min，臭氧投加量需满足要求为:臭氧与沉 淀后上清液接触10 min后，采用静滴法，测得超滤膜池中的胶体与纯水的接触角小于60°。
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