CN205575867U - 一种工业废水处理系统 - Google Patents
一种工业废水处理系统 Download PDFInfo
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- CN205575867U CN205575867U CN201520923351.XU CN201520923351U CN205575867U CN 205575867 U CN205575867 U CN 205575867U CN 201520923351 U CN201520923351 U CN 201520923351U CN 205575867 U CN205575867 U CN 205575867U
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- flocculating
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 17
- 239000010842 industrial wastewater Substances 0.000 title claims abstract description 16
- 239000002351 wastewater Substances 0.000 claims abstract description 51
- 238000004062 sedimentation Methods 0.000 claims abstract description 22
- 230000003311 flocculating Effects 0.000 claims abstract description 21
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 17
- 239000012530 fluid Substances 0.000 claims abstract description 16
- 238000005516 engineering process Methods 0.000 claims abstract description 15
- 241000276438 Gadus morhua Species 0.000 claims abstract description 13
- 235000019516 cod Nutrition 0.000 claims abstract description 13
- 239000012528 membrane Substances 0.000 claims abstract description 10
- 238000000034 method Methods 0.000 claims description 40
- 239000002699 waste material Substances 0.000 claims description 14
- 239000010802 sludge Substances 0.000 claims description 13
- 238000007667 floating Methods 0.000 claims description 8
- 238000001556 precipitation Methods 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 4
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- 230000003851 biochemical process Effects 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L cacl2 Chemical compound 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[Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- 229910001628 calcium chloride Inorganic materials 0.000 description 2
- 239000001110 calcium chloride Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound 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[Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 238000004043 dyeing Methods 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-M fluoride anion Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 2
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- 239000010865 sewage Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound 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Abstract
本实用新型公开了一种工业废水处理系统，包括废水收集过滤装置、A²/O工艺处理系统、压裂液及返排水处理系统、重金属处理系统和膜生物反应器，所述沉淀池废水收集过滤装置与厌氧池或缺氧池相连接，好氧池回流至厌氧池或缺氧池，压裂液及返排水处理系统包括依次连接的气浮装置、有机物吸附装置、去硬度沉淀澄清装置、去SS装置以及除TDS和COD装置，去SS装置回流至气浮装置，重金属处理系统包括一级HELDY‑F絮凝沉降和二级HELDY‑F絮凝沉降处理，对废水进行多重处理，对废水中包含的多种杂质分别去除，提高最后的水质，不受废水浓度变化的影响，且污泥和药剂可减量1/4到1/2，管理维护容易，相关重金属处理后能降至0.1mg/l以下，经济、安全，运行成本低。
Description
技术领域
[0001]本实用新型涉及污泥处理技术领域，特别涉及一种工业废水处理系统。
背景技术
[0002]在工业生产，以及人们的日常生活中，都会产生大量的废水。废水的种类有很多种，例如含N、S及卤素类的有机废水;含酸、碱、氧化剂、还原剂的废水;含石油、动植物性油脂的废水;含有机磷的废水;含酚类物质的废水。
[0003]例如，矿井水是废水中的一种。矿井水是在煤炭开采过程中，地下水与煤层、岩层接触，加上人类活动的影响，在发生了一系列的物理、化学和生化反应后产生的废水。矿井水的水质具有显著的煤炭行业特征:含有的悬浮物的含量远远高于地表水，感官性状差;并且所含悬浮物的粒度小、比重轻、沉降速度慢、混凝效果差;矿井水中还含有废机油、乳化油等有机物污染物。矿井水中含有的总离子含量比一般地表水高得多，而且很大一部分是硫酸根离子。矿井水往往PH值特别低，常伴有大量的亚铁离子，增加了处理的难度。
[0004]在现有的废水处理过程中，尤其是对矿井水的处理中，通常单独使用膜生物反应器(MBR)法或序列间歇式活性污泥法(SBR)或生物接触氧化法或曝气生物滤池(BAF)J^R能对废水进行单一的处理，例如为过滤或微生物反应或去除毒性等。但是废水中包括多种杂质，如固体大颗粒物、细菌、有毒物质等，单一的处理只能对其中的一种或几种杂质进行处理，无法得到质量更佳的水质。
[0005]申请号为CN201410714942.6的中国专利，公开了一种工业印染废水的处理方法，包括预处理、生化处理和深度处理三级结合的处理工序。本发明工业印染废水的处理方法，通过预处理、生化处理和深度处理三级结合的处理工序。其预处理工序采用虹吸排泥式平流池，通过投加絮凝药剂实现无机大分子物质及部分有机悬浮物的混凝沉淀，及初步的泥水分离；并在生化处理过程中利用脉冲式布水布气实现水解酸化与好氧曝气两级生化处理，提高废水的可生化性，改善后续生化处理的条件。为进一步降低废水中悬浮物质及COD等污染物，在深度处理工序中经二沉池处理排放的废水经高效深度处理V型滤池的深度处理，提高废水处理的效果和出水水质，满足中水回用标准，实现废水资源回收利用，符合国家节能排放要求与目标。
实用新型内容
[0006]本实用新型所要解决的技术问题是提供一种工业废水处理系统，以解决现有技术中导致的上述仅采用膜生物反应器对废水进行单一的处理，但废水中包括多种杂质，如固体大颗粒物、细菌、有毒物质等，单一的处理只能对其中的一种或几种杂质进行处理，无法得到质量更佳的水质的缺陷。
[0007]为实现上述目的，本实用新型提供以下的技术方案:一种工业废水处理系统，包括废水收集过滤装置、A2/0工艺处理系统、压裂液及返排水处理系统、重金属处理系统和膜生物反应器，所述废水收集过滤装置、A2/0工艺处理系统、压裂液及返排水处理系统和重金属处理系统为顺序布置，A2/0工艺处理系统包括厌氧池、缺氧池、好氧池和沉淀池，其中厌氧池、缺氧池、好氧池为顺序布置，沉淀池废水收集过滤装置与厌氧池或缺氧池相连接，好氧池回流至厌氧池或缺氧池，压裂液及返排水处理系统包括依次连接的气浮装置、有机物吸附装置、去硬度沉淀澄清装置、去SS装置以及除TDS和COD装置，去SS装置回流至气浮装置，重金属处理系统包括一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理，且有机物吸附装置、去硬度沉淀澄清装置、去SS装置、除TDS和COD装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理均连接至沉淀处理装置。
[0008]优选的，所述废水收集过滤装置采用格栅井，且格栅分为粗格栅和细格栅。
[0009] 优选的，所述工业废水处理系统中设有污泥浓缩池，且沉淀池连接至污泥浓缩池，污泥浓缩池连接有压泥机。
[0010] 优选的，所述去硬度沉淀澄清装置、去SS装置、除TDS和COD装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理的底部均设有搅拌装置。
[0011]优选的，优选的，所述去SS装置内部设有加酸装置。
[0012]采用以上技术方案的有益效果是:本实用新型采用A2/0工艺处理技术、压裂液及返排水处理技术、重金属处理技术和膜生物反应器对废水进行处理，对废水进行多重处理，对废水中包含的多种杂质分别去除，从而可提高最后得到的水质，通过生化法对废水进行了脱氮除磷处理和去除有机物的处理，同时还通过膜生物反应器MBR法对水体中的活性污泥和大分子物质进行截留的处理，与传统废水处理系统相比，效率更高，几乎不受废水浓度变化的影响，运行稳定性高，且污泥和药剂可减量1/4到1/2，费用低，管理维护容易，处理效果好，相关重金属处理后能降至0.lmg/1以下，经济、安全，运行成本低。
附图说明
[0013]图1是本实用新型的结构示意图。
具体实施方式
[0014]下面结合附图详细说明本实用新型的优选实施方式。
[0015]图1出示本实用新型的具体实施方式:一种工业废水处理系统，包括废水收集过滤装置、A2/0工艺处理系统、压裂液及返排水处理系统、重金属处理系统和膜生物反应器，所述废水收集过滤装置、A 2/0工艺处理系统、压裂液及返排水处理系统和重金属处理系统为顺序布置，A2/0工艺处理系统包括厌氧池、缺氧池、好氧池和沉淀池，其中厌氧池、缺氧池、好氧池为顺序布置，沉淀池废水收集过滤装置与厌氧池或缺氧池相连接，好氧池回流至厌氧池或缺氧池，压裂液及返排水处理系统包括依次连接的气浮装置、有机物吸附装置、去硬度沉淀澄清装置、去SS装置以及除TDS和COD装置，去SS装置回流至气浮装置，重金属处理系统包括一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理，且有机物吸附装置、去硬度沉淀澄清装置、去SS装置、除TDS和COD装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理均连接至沉淀处理装置。
[0016]在本实用新型中，所述废水收集过滤装置采用格栅井，且格栅分为粗格栅和细格栅。
[0017]在本实用新型中，所述工业废水处理系统中设有污泥浓缩池，且沉淀池连接至污泥浓缩池，污泥浓缩池连接有压泥机。
[0018]在本实用新型中，所述去硬度沉淀澄清装置、去SS装置、除TDS和⑶D装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理的底部均设有搅拌装置。
[0019]在本实用新型中，所述气浮装置和去硬度沉淀澄清装置内部设有加絮凝剂装置。
[0020]在本实用新型中，所述去SS装置内部设有加酸装置。
[0021]其中，在压裂液及返排水处理系统中，对于高TDS的压裂液及返排水，如选择处理后的回用，考虑除去油脂、细菌和硬度，如选择处理后排放，还需要考虑除去TDS，对于高COD、高TDS的压裂液及返排水，需增加COD的处理。
[0022] HELDY-F系统是一种无机废水的处理系统，一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理均是通过加入石灰、氯化钙和絮凝剂，使废水中的氟化物与石灰和氯化钙中的钙离子生成氟化钙沉淀，以达到去除废水中氟化物的目的，它能够减少处理过程中的污泥产量。该系统能够有效地处理重金属，并特别适用于排放大量的氟废水的生产线，如半导体行业、玻璃行业、印刷行业以及金属制造行业。主要特点与一般絮凝沉淀处理同样的设备，可以完成尚度效率的处理;几乎不受废水浓度变化的影响，具有很尚的运彳丁稳定性;污泥减量效果大，业已证实，特别是处理含氟废水时，污泥减量效果及药剂用量减少，运行成本得以大幅降低;系统简单，管理维护容易。
[0023]采用A2/0工艺处理技术、压裂液及返排水处理技术、重金属处理技术和膜生物反应器对废水进行处理，对废水进行多重处理，对废水中包含的多种杂质分别去除，从而可提高最后得到的水质，通过生化法对废水进行了脱氮除磷处理和去除有机物的处理，同时还通过膜生物反应器MBR法对水体中的活性污泥和大分子物质进行截留的处理，与传统废水处理系统相比，效率更高，几乎不受废水浓度变化的影响，运行稳定性高，且污泥和药剂可减量1/4到1/2，费用低，管理维护容易，处理效果好，相关重金属处理后能降至0.lmg/1以下，经济、安全，运行成本低。
[0024]以上所述的仅是本实用新型的优选实施方式，应当指出，对于本领域的普通技术人员来说，在不脱离本实用新型创造构思的前提下，还可以做出若干变形和改进，这些都属于本实用新型的保护范围。
Claims (6)
1.一种工业废水处理系统，包括废水收集过滤装置、A2/0工艺处理系统、压裂液及返排水处理系统、重金属处理系统和膜生物反应器，其特征在于，所述废水收集过滤装置、A2/0工艺处理系统、压裂液及返排水处理系统和重金属处理系统为顺序布置，A2/0工艺处理系统包括厌氧池、缺氧池、好氧池和沉淀池，其中厌氧池、缺氧池、好氧池为顺序布置，沉淀池废水收集过滤装置与厌氧池或缺氧池相连接，好氧池回流至厌氧池或缺氧池，压裂液及返排水处理系统包括依次连接的气浮装置、有机物吸附装置、去硬度沉淀澄清装置、去SS装置以及除TDS和COD装置，去SS装置回流至气浮装置，重金属处理系统包括一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理，且有机物吸附装置、去硬度沉淀澄清装置、去SS装置、除TDS和⑶D装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理均连接至沉淀处理装置。
2.根据权利要求1所述的一种工业废水处理系统，其特征在于，所述废水收集过滤装置采用格栅井，且格栅分为粗格栅和细格栅。
3.根据权利要求2所述的一种工业废水处理系统，其特征在于，所述工业废水处理系统中设有污泥浓缩池，且沉淀池连接至污泥浓缩池，污泥浓缩池连接有压泥机。
4.根据权利要求3所述的一种工业废水处理系统，其特征在于，所述去硬度沉淀澄清装置、去SS装置、除TDS和COD装置、一级HELDY-F絮凝沉降和二级HELDY-F絮凝沉降处理的底部均设有搅拌装置。
5.根据权利要求4所述的一种工业废水处理系统，其特征在于，所述气浮装置和去硬度沉淀澄清装置内部设有加絮凝剂装置。
6.根据权利要求5所述的一种工业废水处理系统，其特征在于，所述去SS装置内部设有加酸装置。
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