CN107601666A - 一种填料型农村污水一体化处理装置及工艺 - Google Patents
一种填料型农村污水一体化处理装置及工艺 Download PDFInfo
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- CN107601666A CN107601666A CN201710861588.3A CN201710861588A CN107601666A CN 107601666 A CN107601666 A CN 107601666A CN 201710861588 A CN201710861588 A CN 201710861588A CN 107601666 A CN107601666 A CN 107601666A
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- Prior art keywords
- pond
- sewage
- aerobic
- sedimentation basin
- anoxic
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- 239000010865 sewage Substances 0.000 title claims abstract description 109
- 238000000034 method Methods 0.000 title claims abstract description 28
- 238000004062 sedimentation Methods 0.000 claims abstract description 46
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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[P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims abstract description 37
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 37
- 239000011574 phosphorus Substances 0.000 claims abstract description 37
- 239000000835 fiber Substances 0.000 claims abstract description 15
- 230000001360 synchronised Effects 0.000 claims abstract 2
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- 241000894006 Bacteria Species 0.000 claims description 18
- NBIIXXVUZAFLBC-UHFFFAOYSA-K [O-]P([O-])([O-])=O Chemical compound 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[O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 15
- 239000010452 phosphate Substances 0.000 claims description 15
- 238000005273 aeration Methods 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound 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- 230000036961 partial Effects 0.000 claims description 3
- 238000000926 separation method Methods 0.000 claims description 3
- FGIUAXJPYTZDNR-UHFFFAOYSA-N Potassium nitrate Chemical compound 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[K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 23
- 239000002244 precipitate Substances 0.000 abstract description 3
- 239000000945 filler Substances 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract 1
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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Abstract
本发明公开了一种填料型农村污水一体化处理装置及工艺。该装置包括厌氧池(1)、缺氧池(2)、好氧池(3)和沉淀池(4);所述厌氧池(1)、缺氧池(2)、好氧池(3)和沉淀池(4)处于同一壳体内,且每个池通过隔板分隔开,通过在好氧池添加纤维式组合填料(5),增强好氧区的硝化能力。基于该装置的处理工艺包括步骤:(1)厌氧池释磷;(2)缺氧池同步脱氮除磷;(3)好氧池硝化并吸磷;(4)沉淀池沉淀;(5)溢流排水。本发明设备结构简洁,自动化程度高,处理效果好,出水水质稳定,增加填料后通过生物膜的作用硝化效果明显提高,并可节省能耗,适用于农村生活污水的处理以及针对旧设备硝化作用能力不足情况的升级改造。
Description
一种填料型农村污水一体化处理装置及工艺
技术领域
[0001] 本发明属于城市污水处理技术领域,具体涉及一种填料型农村污水一体化处理装 置及工艺。
背景技术
[0002] 伴随着经济的高速发展,城镇化和工业化速度的加快,环境污染问题严重影响着 农村的生态环境,农民的身体健康以及农产品的安全。据莫欣岳Q等人的研宄显示,全国农 村每年产生生活污水约80多亿吨,而96 %的村庄没有排水渠道和污水处理系统,大部分生 活污水未经处理直接排放;生活垃圾因缺乏统一回收处理途径而被随意露天堆放,绝大部 分最终进入水体。这些都导致了农村河流水质急剧下降,直接威胁农村居民的饮用水安全。 根据贺靖°等人对宁夏的调研显示,目前我国对于农村生活污水的主要处理方式为人工湿 地,蚯蚓生物滤池和土壤渗滤技术等,以上处理方法虽可以处理部分的污染物,但是无法达 到《城镇污水处理厂污染物排放标准》一级A标准。(文献出处:[1]莫欣岳,李欢,杨宏,等.新 形势下我国农村水污染现状、成因与对策[J].世界科技研究与发展,2016,38 (5) :1125-1129. [2]贺婧,李小宇,罗玲玲,等.宁夏农村生活污水处理系统现状调查与问题分析[J]. 中国农村水利水电,2016(6) :123-127.)
[0003]反硝化聚磷菌的技术理论是利用反硝化聚磷菌以硝酸盐氮或亚硝酸盐氮为电子 受体,进行同步脱氮除磷。在厌氧,缺氧交替运行的环境中,比较容易富集具有反硝化除磷 作用的兼性微生物。研宄表明,适当扩大缺氧池的体积有利于反硝化聚磷菌的富集,但是在 池体大小固定的条件下,扩大缺氧池的体积间接减小了好氧池的体积,不利于硝化作用的 进行。为了更好的解决农村散户生活污水污染环境的问题,本发明通过增加缺氧混合液回 流,克服了在A2/0中,反硝化聚磷菌不能够得到有效富集的问题,在一定程度上缓解了生物 脱氮和生物除磷直接的矛盾;通过在好氧区添加纤维式组合填料,为微生物附着提供了巨 大的表面积,形成生物膜后强化了好氧区微生物的硝化作用,另外,由于采用生物膜,可以 大大降低农村污水处理的运行成本。
发明内容
[0004]本发明目的针对现有农村污水处理技术不足,所处理的生活污水无法达到《城镇 污水处理厂污染物排放标准》一级A标准。目前农村生活污水主要通过沼气池,生态滤池等 方法进行处理,其问题在于占地面积大,处理效果较差。在不增加反应器体积的前提下,设 计开发出占地面积小,工艺简洁,可充分利用碳源,高效脱氮除磷的一种填料型农村污水一 体化处理装置。
[0005] 本发明还提供基于所述设备的填料型农村污水一体化处理工艺。
[0006] 本发明目的通过如下技术方案实现。
[0007] —种填料型农村污水一体化处理装置,包括厌氧池、缺氧池、好氧池和沉淀池;所 述厌氧池、缺氧池、好氧池和沉淀池处于同一壳体内,且每个池通过隔板分隔开;
[0008] 所述好氧池分为第一好氧池和第二好氧池;
[0009] 所述厌氧池与缺氧池通过隔板分隔开,分隔厌氧池与缺氧池的隔板底部设置有第 一过水涧,污水处理过程中的污水通过第一过水涧从厌氧池流入缺氧池;
[0010] 所述缺氧池与第一好氧池通过隔板分隔开,分隔缺氧池与第一好氧池的隔板的中 部设置有第二过水涧,污水处理过程中的污水通过第二过水涧从缺氧池流入第一好氧池; 分隔第一好氧池与第二好氧池的隔板设置有第三过水润,污水处理过程中的污水通过第三 过水涧从第一好氧池流入第二好氧池;
[0011] 所述沉淀池与第二好氧池通过隔板分隔开,分隔沉淀池与第二好氧池的隔板中上 部设置有布水管,且布水管均匀分布于同一平面上,污水处理过程中的污水通过布水管从 第二好氧池向沉淀池垂直向下进水,保证沉淀池的沉淀效率;
[0012] 所述厌氧池的底部设置有第一机械搅拌装置;所述缺氧池的底部设置有第一曝气 头和第二机械搅拌装置;所述缺氧池还设置有排空口;所述缺氧池还通过第一回流管道和 第一回流泵与厌氧池连接;
[0013] 所述第一好氧池和第二好氧池的底部均设置有均匀排布的第二曝气头,每排曝气 头均通过单独气阀控制曝气量;所述第二好氧池还通过第二回流管道和第二回流栗与缺氧 池连接;
[0014] 所述第一好氧池和第二好氧池的设置有均匀排布的纤维式组合填料。
[0015] 所述沉淀池为平流式沉淀池;所述沉淀池底部设置有3个集泥斗;所述集泥斗平行 于水流方向,且各集泥斗内部均分别插入一排泥管;所述排泥管垂直于水流方向;排泥管一 端均伸出沉淀池的底部,伸出端合并为一个出口后通过三通连通,三通的一条通道与排泥 井连通,三通的另一条通道通过第三回流管和第三回流泵与厌氧池连接;
[0016] 三条排泥管合三为一既有利于均匀排泥,又方便操作,避免了污泥在三个集泥斗 中不均匀分布而导致出水悬浮物升高;
[0017] 设备的进水口设置在厌氧池前端,设备的出水口设置在沉淀池的后端,靠近设备 出水口处设置有出水堰,出水堰前设置有挡板以截留水面浮渣。
[0018] 进一步地,所述集泥斗为倒棱台状,上底与下底的长度比为2:1;倒棱台的形状可 以有效地集中污泥,避免产生排泥死角,从而导致因池体污泥残留使得二沉池反硝化以致 污泥上浮,影响工艺的出水稳定性。
[0019] 进一步地,所述出水堰的形状为锯齿状。
[0020] 进一步地,所述好氧池中第二好氧池纤维式组合填料的分布比第一好氧池中的分 布密集。
[0021] 进一步地,所述第二好氧池末端出水中的溶解氧在l_〇mg/L-1.5mg/L之间。
[0022]进一步地,所述排泥管插入集泥斗的部分等距离开均匀开有小孔,有利于集泥斗 中的污泥均匀的流入排泥管中,不会形成因排泥不均匀而导致的污泥残留、堆积。
[0023] 进一步地,所述厌氧池内通过缺氧-厌氧回流富集含有反硝化聚磷菌;所述缺氧池 内含有反硝化细菌和反硝化聚磷菌;所述好氧池内含有硝化菌和反硝化聚磷菌。
[0024] 基于上述设备的填料型农村污水一体化处理工艺,包括如下步骤:
[0025] (1)厌氧池释磷:农村生活污水通过进水口进入厌氧池,在厌氧池中通过反硝化聚 磷菌完成释磷;
[0026] (2)缺氧池反硝化脱氮:厌氧池释磷后的污水通过第一过水涧进入缺氧池,缺氧池 中的反硝化细菌利用污水中的COD作为碳源对硝酸盐进行反硝化,实现脱氮;
[0027] (3)好氧池硝化吸磷:缺氧池中脱氮后的污水按回流比120%-150%通过第一回流 管道和第一回流泵回流至厌氧池,剩余的污水通过第二过水涧进入好氧池,在好氧池中硝 化细菌的硝化作用下,氨氮转化为硝酸盐态的氮,并完成好氧吸磷;
[0028] ⑷沉淀池沉淀:好氧池硝化作用后的污水按回流比200%通过第二回流管道和第 二回流泵从第二好氧池回流至缺氧池,剩余的污水通过布水管流入沉淀池中,污水在沉淀 池中平流,并由于污泥自身重力完成污泥沉淀;
[0029] (5)溢流排水:沉淀池中沉淀的污泥通过集泥斗收集后,污泥按回流比70%-80% 通过第三回流管和第三回流泵回流至厌氧池,剩余的污泥排入排泥井;泥水分离后的处理 水通过出水堰溢流并从出水口排出。
[0030]与现有技术相比,本发明具有如下优点和有益效果:
[0031] (1)本发明设备构造简洁,易于操作,占地面积小;每个池在同一壳体内完成,便于 管理;且沉淀池利用重力进行泥水的有效分离不需增加运行耗能,降低了运行成本;
[0032] (2)本发明增加了反硝化聚磷菌在厌氧池的停留时间,并且降低了硝酸盐在厌氧 池对反硝化聚磷菌释磷的影响;
[0033] (3)本发明针对农村生活污水低碳源的特点,充分利用污水中的C0D,并缓解了聚 磷菌和反硝化细菌的竞争关系,提高了脱氮除磷的效率;
[0034] (4)本发明在好氧池中增加纤维式组合填料,挂膜成功后有效地提高了硝化作用 的效率。
[0035] (5)基于本发明设备的水处理工艺对C0D、TP和TN的处理效果较好,出水COD可达到 20mg/L以下,总磷出水0 • 5mg/L以下,出水氨氮2 • Omg/L以下,各项出水水质指标均达到并高 于《城镇污水处理厂污染物排放标准》一级A标准。
附图说明
[0036]图1为本发明一种填料型农村污水一体化处理装置的平面结构示意图 [0037]图2为实施例1中处理实际污水对C0D的去除效果图;
[0038]图3为实施例1中处理实际污水对氨氮的去除效果图; t〇〇39]图4为实施例1中处理实际污水对总氮的去除效果图;
[0040]图5为实施例1中处理实际污水对总磷的去除效果图。
具体实施方式
[0041]以下结合附图和实施例对本发明作进一步说明,但本发明所要求保护的范围并不 局限于具体实施方案中所描述的范围。
[0042] 本发明一种填料型农村污水一体化处理装置的结构示意图如图1所示,依次包括 厌氧池1、缺氧池2、好氧池和沉淀池4;厌氧池1、缺氧池2、好氧池和沉淀池4处于同一壳体 内,且每个池通过隔板分隔开;好氧池分为第一好氧池3-1和第二好氧池3-2;厌氧池1内含 有反硝化聚磷菌;缺氧池2内含有反硝化细菌和反硝化释磷菌;好氧池内含有硝化菌和反硝 化聚磷菌;
[0043] 厌氧池1与缺氧池2通过隔板分隔开,分隔厌氧池1与缺氧池2的隔板底部设置有第 一过水涧7,污水处理过程中的污水通过第一过水涧7从厌氧池1流入缺氧池2;
[0044] 缺氧池2与第一好氧池3-1通过隔板分隔开,分隔缺氧池2与第一好氧池3-1的隔板 的中部设置有第二过水涧8,污水处理过程中的污水通过第二过水涧8从缺氧池2流入第一 好氧池3-1;
[0045] 分隔第一好氧池3-1与第二好氧池3-2的隔板设置有第三过水涧9,污水处理过程 中的污水通过第三过水涧9从第一好氧池3-1流入第二好氧池3-2;所述第一好氧池3-1和第 二好氧池3-2的设置有均匀排布的纤维式组合填料5。
[0046] 沉淀池4与第二好氧池3-2通过隔板分隔开,分隔沉淀池4与第二好氧池3-2的隔板 中上部设置有布水管10,且布水管10均匀分布于同一平面上,污水处理过程中的污水通过 布水管10从第二好氧池3-2向沉淀池4垂直向下进水;
[0047] 厌氧池1的底部设置有第一机械搅拌装置11;缺氧池2的底部设置第二机械搅拌装 置12;缺氧池2还设置有排空口 I3;缺氧池2还通过第一回流管道14和第一回流泵15与厌氧 池1连接;
[0048] 第一好氧池3-1和第二好氧池3_2的底部均设置有均匀排布的曝气头16,每排曝气 头均通过单独气阀控制曝气量;第二好氧池3-2还通过第二回流管道17和第二回流泵18与 缺氧池2连接;
[0049]沉淀池4为平流式沉淀池;沉淀池4底部设置有3个集泥斗;集泥斗为倒棱台状,上 底与下底的长度比为2:1;集泥斗平行于水流方向,且各集泥斗内部均分别插入一排泥管; 排泥管插入集泥斗的部分等距离开均匀开有小孔;排泥管2〇垂直于水流方向;3条排泥管一 端均伸出沉淀池4的底部,伸出端合并为一个出口后通过三通连通,三通的一条通道与排泥 井21连通,三通的另一条通道通过第三回流管22和第三回流栗23与厌氧池1连接;
[0050] 设备的进水口 6设置在厌氧池1前端,设备的出水口 24设置在沉淀池4的后端,靠近 设备出水口处设置有出水堰25,出水堰25的形状为锯齿状。
[0051] 实施例1
[0052] 采用上述填料型农村污水一体化处理装置处理进行农村生活污水的处理,设备整 体实用钢板质地,装置内部隔板使用4mm钢板,外部站板使用6mm钢板,底板采用8mm钢板,装 置焊缝采用双面焊,去除毛刺飞边,无渗漏。
[0053] 处理工艺包括如下步骤:
[0054] (1)农村生活污水通过进水口 6进入厌氧池1,在厌氧池1中通过释磷菌完成释磷;
[0055] (2)厌氧池1释磷后的污水通过第一过水涧7进入缺氧池2,缺氧池2中的反硝化细 菌利用污水中的C0D作为碳源对硝酸盐进行反硝化,实现脱氮;
[0056] ⑶缺氧池2脱氮后的污水按回流比15〇%通过第一回流管道14和第一回流泵15回 流至厌氧池,剩余的污水通过第二过水涧8进入好氧池,在硝化细菌的硝化作用下,氨氮转 化为硝酸盐态的氮,并完成好氧吸磷;
[0057] ⑷好氧池硝化作用后的污水通过第二回流管道17和第二回流栗18从第二好氧池 3-2回流至缺氧池,剩余的污水通过布水管流入沉淀池4中,污水在沉淀池4中平流并完成污 泥沉淀;
[0058] (5)沉淀池4中沉淀的污泥通过集泥斗收集后,污泥回流通过第三回流管22和第三 回流栗23回流至厌氧池1,剩余的污泥排入排泥井;泥水分离后的处理水通过出水堰25溢流 并从出水口 24排出。
[0059] 农村生活污水的平均进水氨氮浓度为27.38mg/L,平均进水总氮浓度为32.74mg/ L,平均进水总磷浓度为3 • 65mg/L,平均进水COD浓度为241 • 20mg/L;污水在整个一体化设备 的水力停留时间为8h。
[0060] 对比添加纤维式组合填料前后装置对于氨氮,总氮,总磷,COD的去除效果,每个工 况考察期为30d,单因素实验结果如下:
[0061] (1)在无添加纤维式组合填料的条件下,运行条件为:缺氧池混合液回流比R = 150 %,好氧池混合液回流比心=200 %,污泥回流比R2 = 80%,污水进入厌氧池的流速为 2m3/h,污水在整个一体化设备的水力停留时间为8h;当缺氧池体积增大的条件下,运行稳 定后,氨氮的平均去除率为85 • 33 %,总氮的平均去除率为61.79 %,总磷的平均去除率为 85 • 46%,C0D的平均去除率为90.31 %。
[0062] (2)在添加纤维式组合填料的条件下,运行条件为:缺氧池混合液回流比R二 150 %,好氧池混合液回流比心=200 %,污泥回流比R2 = 80%,污水进入厌氧池的流速为 2m3/h,污水在整个一体化设备的水力停留时间为8h;当缺氧池体积增大的条件下,运行稳 定后,氨氮的平均去除率为90.47%,总氮的平均去除率为70.96%,总磷的平均去除率为 86.48%,C0D的平均去除率为92.46%。
[0063]实施效果
[0064] 根据以上单因素实验考察填料型农村污水一体化处理装置的处理结果,当处理量 为48Vd,缺氧池混合液回流比R= 150%,好氧池混合液回流比1^ = 200%,污泥回流比R2 = 80%,污水进入厌氧池的流速为2m3/h,污水在整个一体化设备的水力停留时间为8h,考察 农村生活污水一体化处理设备处理污水的处理效果,考察时间为30d。
[0065] 1、C0D的去除效果
[0066] C0D的去除效果如图4所示,由图4可知,进入装置的污水中C0D浓度较低,其中进水 最高C0D浓度为324mg/L,进水最低C0D浓度为135mg/L,平均进水C0D浓度为200.3mg/L;而出 水C0D最高浓度为25. lmg/L,最低COD浓度为8.5mg/L,平均出水C0D浓度为14.29mg/L,平均 去除率为92.46 %,远优于《城镇污水处理厂污染物排放标准》一级A标准。
[0067] COD是污水处理工艺中微生物生长的碳源,在进行污水的脱氮除磷作用时,反硝化 脱氮菌属于异养型兼性厌氧菌,在缺氧条件时,以有机碳为电子供体和营养源进行反硝化 反应;而实现除磷作用的聚磷菌需要主动吸收由厌氧发酵产酸菌转化水中有机物成为的乙 酸苷,这也会消耗碳源。
[0068] 基于本发明农村生活污水一体化处理设备的工艺对于COD具有非常好的去除效 果,其中的碳源已经被高效的利用。
[0069] 2、氨氮和总氮的去除效果
[0070]氨氮的去除效果如图2,由图2可知,进入装置的污水的总氮以氨氮为主,其中进水 最高氨氮浓度为35.12mg/L,进水最低氨氮浓度为20.73mg/L,平均进水氨氮浓度为 27.39mg/L;经过好氧池活性污泥中硝化细菌的硝化作用后,其出水氨氮最高浓度为 3 • 92mg/L,最低氨氮浓度为1 • 07mg/L,平均出水氨氮浓度为2 • 95mg/L,平均氨氮去除率为 90.47 %,远优于《城镇污水处理厂污染物排放标准》一级A标准。 L〇〇71J总熟的去除效果如图3所示,由图3可知,进水最高总氮浓度为39.35mg/L,进水最 低总氮浓度为22.30mg/L,平均进水总氮浓度为3l_34mg/L,经过微生物的反硝化脱氮过程 后,其出水总氮最高浓度为K.Olmg/L,最低总氮浓度为5.98mg/L,平均出水总氮浓度为 8.99mg/L,平均总氮去除率为70 • % %,优于《城镇污水处理厂污染物排放标准》一级A标准。 [0072]可见本发明脱氮效果优异,且对比起无添加纤维式组合填料而言,氨氮的去除率 由85.33糾是髙到90.47%,总氮去除率由61.79%提高到7〇. 96%。这是由于添加纤维式组 合填料后,组合填料为硝化细菌提供了较大的栖息空间,挂膜成功后,强化了好氧区的硝化 作用。与此同时,其巨大的比表面积使得硝化细菌对氧气的利用率有所提高,减少了好氧回 流对缺氧区的不利影响,提高了反硝化作用的效率。
[0073] 3、总磷的去除效果
[0074]总磷的去除效果如图5所示,由图5可知,进入装置的污水中总磷浓度波动较大,其 中进水最高总磷浓度为5.84mg/L,进水最低总磷浓度为2.22mg/L,平均进水总磷浓度为 3.66mg/L;而出水总磷最高浓度为〇. 49mg/L,最低总磷浓度为0.36mg/L,平均出水总磷浓度 为0 • 45mg/L,平均去除率为86.74%,达到《城镇污水处理厂污染物排放标准》一级A标准。 [0075]基于本发明农村生活污水一体化处理设备的工艺对于总磷具有非常好的去除效 果。
[0076]综上所述本发明农村生活污水一体化处理设备以及工艺对目标污染物COD,总氮, 总磷有很好的去除效果,其中平均出水⑶D浓度为14 • 29mg/L,平均出水总氮浓度为8 • 99mg/ L,平均出水总磷浓度为0 • 45mg/L,各项出水达到并优于《城镇污水处理厂污染物排放标准》 一级A标准。
Claims (10)
1. 一种填料型农村污水一体化处理装置,其特征在于,包括厌氧池(1)、缺氧池(2)、好 氧池和沉淀池(4);所述厌氧池(1)、缺氧池(2)、好氧池和沉淀池(4)处于同一壳体内且通过 隔板分隔开; 所述好氧池分为第一好氧池(3-1)和第二好氧池(3-2); 所述厌氧池(1)与缺氧池(2)通过隔板分隔开,分隔厌氧池(1)与缺氧池(2)的隔板底部 设置有第一过水涧(7),污水处理过程中污水先经过进水口(6)进入厌氧池,再通过第一过 水涧(7)从厌氧池(1)流入缺氧池(2); 所述缺氧池(2)与第一好氧池(3-1)通过隔板分隔开,分隔缺氧池(2)与第一好氧池(3- 1) 的隔板的中部设置有第二过水涧(8),污水处理过程中的污水通过第二过水涧(8)从缺氧 池(2)流入第一好氧池(3-1); 所述第一好氧池(3-1)与第二好氧池(3-2)的隔板设置有第三过水涧(9),污水处理过 程中的污水通过第三过水涧(9)从第一好氧池(3-1)流入第二好氧池(3-2); 所述沉淀池(4)与第二好氧池(3-2)通过隔板分隔开,分隔沉淀池(4)与第二好氧池(3- 2) 的隔板中上部设置有布水管(10),且布水管(10)于同一水平面均匀分布,污水处理过程 中的污水通过布水管(10)从第二好氧池(3-2)向沉淀池(4)垂直向下进水; 所述厌氧池(1)的底部设置有第一推流式搅拌器(11);所述缺氧池(2)的底部设置第二 推流式搅拌器(12);所述缺氧池(2)还设置有排空口(13);所述缺氧池(2)还通过第一回流 管道(14)和第一回流泵(15)与厌氧池(1)连接; 所述第一好氧池(3-1)和第二好氧池(3-2)的底部均设置有均匀排布的曝气头(16);所 述第一好氧池(3-1)和第二好氧池(3-2)的设置有均匀排布的纤维式组合填料(5);所述第 二好氧池(3-2)还通过第二回流管道(17)和第二回流泵(18)与缺氧池(2)连接; 所述沉淀池(4)为平流式沉淀池;所述沉淀池(4)底部设置有集泥斗(19);所述集泥斗 垂直于水流方向,且各集泥斗内部均分别插入一排泥管(20);所述排泥管(20)垂直于水流 方向;排泥管(20)—端均伸出沉淀池(4)的底部,伸出端与三通连接,三通的一条通道与排 泥井(21)连通,三通的另一条通道通过第三回流管(22)和第三回流泵(23)与厌氧池(1)连 接; 设备的出水口(24)设置在沉淀池(4)的后端,靠近设备出水口(24)处设置有出水堰 (25)〇
2. 根据权利要求1所述的一种填料型农村污水一体化处理装置,其特征在于,所述集泥 斗为倒棱台状,上底与下底的长度比为2:1;所述出水堰(25)的形状为锯齿状。
3. 根据权利要求1所述的一种填料型农村污水一体化处理装置,其特征在于,所述好氧 池中添加有纤维式组合填料(5)。
4. 根据权利要求1所述的一种填料型农村污水一体化处理装置,其特征在于,所述第二 好氧池(3-2)所添加的纤维式组合填料(5)比第一好氧池(3-1)密度更大。
5. 根据权利要求1所述的一种填料型农村污水一体化处理装置,其特征在于,所述排泥 管(20)插入集泥斗的部分等距离均匀开有小孔。
6. 根据权利要求1或5所述的一种填料型农村污水一体化处理装置,其特征在于,所述 沉淀池(4)底部设置的集泥斗(19)有3条;各集泥斗内部均分别插入排泥管(20) ; 3条排泥管 (20) —端均伸出沉淀池(4)的底部,伸出端合并为一个出口后通过三通连通,三通的一条通 道与排泥井(21)连通,三通的另一条通道通过第三回流管(22)和第三回流栗(23)与厌氧池 (1)连接。
7.根据权利要求1所述的一种填料型农村污水一体化处理装置,其特征在于,所述厌氧 池(1)内通过缺氧-厌氧回流富集含有反硝化聚磷菌;所述缺氧池(2)内含有反硝化细菌和 反硝化聚磷菌;所述好氧池内含有硝化细菌和反硝化聚磷菌,所述纤维式组合填料(5)为硝 化细菌提供了栖息场所,其生物膜上含有硝化细菌。
8. 基于权利要求1〜7任一项所述一种填料型农村污水一体化处理装置的处理工艺,其 特征在于,包括如下步骤: (1) 农村生活污水通过进水口(6)进入厌氧池(1),在厌氧池(1)中通过反硝化聚磷菌完 成释磷; (2) 厌氧池(1)释磷后的污水通过第一过水涧(7)进入缺氧池(2),缺氧池(2)中的反硝 化细菌以污水中的COD作为碳源对硝酸盐进行反硝化,实现脱氮;与此同时,反硝化聚磷菌 吸磷,实现同步脱氮除磷; (3) 缺氧池(2)中脱氮后的污水按回流比120 %_150%通过第一回流管道(14)和第一回 流栗(15)回流至厌氧池(1),剩余的污水通过第二过水涧(8)进入好氧池,在好氧池中硝化 细菌的硝化作用下,氨氮转化为硝酸盐态的氮,并在聚磷菌的作用下完成好氧吸磷; (4) 好氧池硝化作用后的污水按回流比200%通过第二回流管道(17)和第二回流栗(18) 从第二好氧池(3-2)回流至缺氧池(2),剩余的污水通过布水管(10)流入沉淀池(4)中,污水 在沉淀池(4)中平流并完成污泥沉淀; (5) 沉淀池(4)中沉淀的污泥通过集泥斗收集后,污泥按回流比70%-80%通过第三回 流管(22)和第三回流泵(23)回流至厌氧池(1),剩余的污泥排入排泥井(21);泥水分离后的 处理水通过出水堰(25)溢流并从出水口(24)排出。
9. 根据权利要求8所述的填料型农村污水一体化处理装置处理工艺,其特征在于,步骤 (1)中,污水进入厌氧池⑴的流量为1.8-2 m3/h。
10. 根据权利要求8所述的填料型农村污水一体化处理装置,其特征在于,污水在整个 一体化设备的水力停留时间为8 h。
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CN112876003A (zh) * | 2021-04-01 | 2021-06-01 | 生态环境部华南环境科学研究所 | 一种处理农村污水的装置 |
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