CN205061792U - 高盐分低碳氮比化工废水的脱氮系统 - Google Patents
高盐分低碳氮比化工废水的脱氮系统 Download PDFInfo
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- CN205061792U CN205061792U CN201520677802.6U CN201520677802U CN205061792U CN 205061792 U CN205061792 U CN 205061792U CN 201520677802 U CN201520677802 U CN 201520677802U CN 205061792 U CN205061792 U CN 205061792U
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- 239000002351 wastewater Substances 0.000 title claims abstract description 32
- 238000005039 chemical industry Methods 0.000 title claims abstract description 18
- 239000011780 sodium chloride Substances 0.000 title abstract description 6
- -1 carbon -nitrogen Chemical compound 0.000 title abstract 2
- 150000003839 salts Chemical class 0.000 title abstract 2
- 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 claims abstract description 72
- 239000010802 sludge Substances 0.000 claims abstract description 39
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 238000006460 hydrolysis reaction Methods 0.000 claims description 22
- 230000020477 pH reduction Effects 0.000 claims description 22
- 238000005188 flotation Methods 0.000 claims description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 17
- 229910052799 carbon Inorganic materials 0.000 claims description 17
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O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 239000010865 sewage Substances 0.000 abstract description 21
- 230000000694 effects Effects 0.000 abstract description 14
- 244000005700 microbiome Species 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 10
- 241000276438 Gadus morhua Species 0.000 description 9
- 235000019516 cod Nutrition 0.000 description 9
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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- 230000037250 Clearance Effects 0.000 description 3
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Abstract
本实用新型公开了一种高盐分低碳氮比化工废水的脱氮系统(20)，包括UC模块单元(17)、气浮池(3)、HBF模块单元(18)、备用系统单元(19)和排放系统(20)，所述UC模块单元(17)、气浮池(3)、HBF模块单元(18)、备用系统单元(19)和排放系统(20)依次相连接；所述UC模块单元(17)、HBF模块单元(18)和备用系统单元(19)分别与污泥浓缩单元(16)相连接。本实用新型的结构流程简单，灵活，配水均匀，具有良好的微生物、污水反应体系，处理效果更高效，而且投资省，自动化程度高。
Description
技术领域
[0001] 本实用新型设计环保污水处理领域，特别是一种高盐分低碳氮比化工废水的脱氮 系统。
背景技术
[0002] 高盐分情况下、低碳氮比的化工废水属于难处理的工业废水，大量氨氮废水排入 水体不仅引起水体富营养化，甚至对人群及生物产生毒害作用。多数情况下C/N比较低，给 氨氮的无害化处理带来困难。传统生物脱氮方法在废水脱氮方面起到了一定的作用，但仍 存在许多问题。如：氨氮完全硝化需消耗大量的氧，增加了动力消耗；对C/N比低的废水，需 外加有机碳源；工艺流程长，占地面积大，基建投资高等。 实用新型内容
[0003] 本实用新型的目的就是为了弥补现有技术的缺陷，提供一种处理效果好的高盐分 低碳氮比化工废水的脱氮系统。
[0004] 为解决上述技术问题，本实用新型提供了一种高盐分低碳氮比化工废水的脱氮系 统，所述高盐分低碳氮比化工废水的脱氮系统包括UC模块单元、气浮池、HBF模块单元、备 用系统单元和排放系统，所述UC模块单元、气浮池、HBF模块单元、备用系统单元和排放系 统依次相连接；所述UC模块单元、HBF模块单元和备用系统单元分别与污泥浓缩单元相连 接。
[0005] 进一步地，所述UC模块单元包括依次相连接的点对点布水器和上流式水解酸化 池；所述点对点布水器和上流式水解酸化池分别与气浮池相连接；所述HBF模块单元包括 污水栗、前置缺氧池、好氧池、后置缺氧池和序批式沉淀池，所述前置缺氧池、好氧池、后置 缺氧池和序批式沉淀池依次相连接；所述备用系统单元包括依次相连接的中间水池、过滤 器和清水池，所述污泥浓缩单元包括依次相连接的浓缩池和脱水机；所述排放系统包括干 污泥外运口和达标水排放口；所述污泥浓缩单元与干污泥外运口相连接；所述备用系统单 元与达标水排放口相连接。
[0006] 进一步地，所述上流式水解酸化池设有36根配水软管，所述点对点布水器通过配 水软管和上流式水解酸化池底部相连接；所述上流式水解酸化池从底部到上部依次设置有 污泥床反应区、稠合沉淀反应区和澄清区。
[0007] 更进一步地，所述好氧池内设置有溶氧仪；所述序批式沉淀池包括第一序批式沉 淀池和第二序批式沉淀池；所述第一序批式沉淀池和第二序批式沉淀池分别通过污水栗与 后置缺氧池相连接。
[0008] 进一步地，所述好氧池、第一序批式沉淀池和第二序批式沉淀池内分别设置有酶 浮填料和曝气装置；所述曝气装置包括射流曝气器和射流循环栗，所述射流曝气器与射流 循环栗相连接。
[0009] 进一步地，所述过滤器为石英砂过滤器。
[0010] 更进一步地，所述浓缩池为重力浓缩池或气浮池；所述脱水机为板框脱水机或带 式脱水机。
[0011] 本实用新型的有益效果：
[0012] 本实用新型的系统，流程简单，灵活，配水均匀，具有良好的微生物、污水反应体 系，处理效果更高效，而且投资省，自动化程度高。
[0013] 本实用新型的优点：
[0014] (1)适用于高盐分废水：经过调试后整个系统中，生物相中的活性污泥和生物膜 能适应含高盐分的工业废水，NaCl含量可达到10000mg/L至12000mg/L，而Na2S04含量可 达到 8000mg/L 至 10000mg/L。
[0015] (2)适用于低C/N比废水：系统中增加 UC模块反应器，可以有效地提高系统的可 生化性，而HBF模块反应器可以加强脱氮效果。因此，常规脱氮系统只有在C/N多4:1才会 对NH 3-N有较好的去除效果；本系统工艺对于4:1多C/N多2:1，也有极佳的效果。当系统 BOD浓度约为130mg/L，出水NH3-N浓度小于10mg/L。
附图说明
[0016] 图1为本实用新型一实施例的工艺流程图；
[0017] 图2为本实用新型的UC模块单元图；
[0018] 图3为本实用新型的HBF模块单元图；
[0019] 其中，1点对点布水器、2上流式水解酸化池、3气浮池、4前置缺氧池、5好氧池、6 后置缺氧池、7第一序批式沉淀池、8第二序批式沉淀池、9中间水池、10过滤器、11清水池、 12达标水排放口、13浓缩池、14脱水机、15干污泥外运口、16污泥浓缩单元、17UC模块单 元、18HBF模块单元、19备用系统单元、20排放系统。
具体实施方式
[0020] 以下通过实施例进一步说明本实用新型。应该理解的是，这些实施例是本实用新 型的阐释和举例，并不以任何形式限制本实用新型的范围。
[0021] 实施例1
[0022] 如图1至图3所示，本实用新型提供了一种高盐分低碳氮比化工废水的脱氮系统。 所述高盐分低碳氮比化工废水的脱氮系统包括UC模块单元17、气浮池3、HBF模块单元18、 备用系统单元19和排放系统20,所述UC模块单元17、气浮池3、HBF模块单元18、备用系 统单元19和排放系统20依次相连接；所述UC模块单元17、HBF模块单元18和备用系统单 元19分别与污泥浓缩单元16相连接。
[0023] 所述UC模块单元17包括依次相连接的点对点布水器1和上流式水解酸化池2 ;所 述点对点布水器1和上流式水解酸化池2分别与气浮池3相连接；所述HBF模块单元18包 括污水栗、前置缺氧池4、好氧池5、后置缺氧池6和序批式沉淀池，所述前置缺氧池4、好氧 池5、后置缺氧池6和序批式沉淀池依次相连接；所述备用系统单元19包括依次相连接的 中间水池9、过滤器10和清水池11，所述污泥浓缩单元16包括依次相连接的浓缩池13和 脱水机14 ;所述排放系统20包括干污泥外运口 15和达标水排放口 12 ;所述污泥浓缩单元 16与干污泥外运口 15相连接；所述备用系统单元19与达标水排放口 12相连接。
[0024] 所述上流式水解酸化池2设有36根配水软管，所述点对点布水器1通过配水软管 和上流式水解酸化池2底部相连接；所述上流式水解酸化池2从底部到上部依次设置有污 泥床反应区、稠合沉淀反应区和澄清区。
[0025] 所述序批式沉淀池包括第一序批式沉淀池7和第二序批式沉淀池8 ;所述第一序 批式沉淀池7和第二序批式沉淀池8分别通过污水栗与后置缺氧池6相连接。
[0026] 所述好氧池5、第一序批式沉淀池7和第二序批式沉淀池8内分别设置有酶浮填料 和曝气装置；所述曝气装置包括射流曝气器和射流循环栗，所述射流曝气器与射流循环栗 相连接。
[0027] 所述过滤器10为石英砂过滤器。
[0028] 所述浓缩池13为重力浓缩池或气浮池；所述脱水机14为板框脱水机或带式脱水 机。
[0029] 本实用新型的高盐分低碳氮比化工废水的脱氮系统的处理方法，包括以下步骤：
[0030] 步骤一、二级生化出水经过重力浓缩后，进入UC模块单元17,污水先进入点对点 布水器1，并通过配水软管进入上流式水解酸化池2的底部，反应后的污水通过出水堰进入 气浮池3 ;要求二级生化废水盐分的浓度不高于10000mg/L，C/N不高于3. 5,进水指标为 COD 为 250mg/L 至 300mg/L，BOD 不低于 150mg/L，NH3-N 的范围处于 100mg/L 至 200mg/L。
[0031] 步骤二、所述UC模块单元17出水经过气浮池3,所述点对点布水器1和上流式水 解酸化池2分别与气浮池3相连接；将UC模块单元17出水中未完全隔离的厌氧污泥重新 流至上流式水解酸化池2内；气浮池3内不添加任何混凝剂以及助凝剂；废水流经点对点 布水器1，被均匀分配至定期测定DO值，要求严格控制厌氧状态；上升流速：池内上升流速 应控制在0. 5m/h以下。此外，控制添加盐酸或氢氧化钠溶液必须保证上流式水解酸化池2 内废水pH值在6. 5-8. 5之间。
[0032] 步骤三、所述气浮池3内的出水流入HBF模块单元18中的前置缺氧池4,硝化液回 流栗设置于好氧池5与缺氧池4之间，所述硝化液回流栗的输入端与好氧池5相连接，所 述硝化液回流栗的输出端与缺氧池4相连接；硝化液回流栗回流输送的液体在前置缺氧池 4进行搅拌混合，同时在其中加入硝态氮进行反硝化反应，将NH3-N则被氧化成N03-N ;
[0033] 所述前置缺氧池4的出水流入好氧池5,其中大部分化学需氧量COD被生物降解， 所述好氧池5内设置有活性污泥、酶浮填料和生物膜，所述生物膜设置在活性污泥和酶浮 填料上部；好氧池内有活性污泥和酶浮填料，活性污泥中含有微生物群落，酶浮填料上也 负载生物膜，生物膜是一种微生物群落。
[0034] 所述好氧池5的出水再流入后置缺氧池6,其中废水的未被完全反硝化进一步反 硝化，N03-N反硝化为N2 ;污水交替进入所述第一序批式沉淀池7和第二序批式沉淀池8， 而批式沉淀池内的剩余污水回流部分污泥至前置缺氧池4 ;HBF模块单元的缺氧池6,硝化 液回流量控制在进水量的300%至400%，维持污泥浓度在400011^/1至500011^/1，剩余污 泥及时排至污泥浓缩池；HBF模块单元的好氧池5内设置有溶氧仪，调节进气量，保证池内 溶解氧浓度为2mg/L至3. 5mg/L ;好氧池5内设置有pH计，可以自动启停加碱栗，维持池内 pH 为 6-9。
[0035] 步骤四、所述HBF模块单元18的出水流入备用系统单元19中的中间水池9，清水 池（11)暂存过滤器10出水，并且清水池11为过滤器10提供反冲洗水，其余水由达标水排 放口 12排出；中间水池9上部设置有溢流孔，HBF模块单元18出水水质稳定时，无需过滤 器10,废水可通过溢流孔溢流至清水池11。而在过滤器10内则是通过过滤作用，去除废水 中细小悬浮物及杂质，降低废水的SS指标。
[0036] 步骤五、流经所述UC模块单元17、HBF模块单元18以及备用系统单元19的剩余 污泥，流入污泥浓缩单元16,通过浓缩池13浓缩后，进入脱水机14,脱水后经干污泥外运口 15排出污泥。
[0037] 在步骤一中，上流式水解酸化池2从底部到上部依次设置有污泥床反应区、稠合 沉淀反应区和澄清区；所述污泥在污泥床反应区进行反应，然后污水缓慢上升，依次经过稠 合沉淀反应区和澄清区，最终污水通过出水堰进入气浮池3。
[0038] 如表1所示，为某污水处理厂使用本实用新型中UC模块单元-气浮池，在第1天 至第24天的进水和出水处理前后数据对比情况。
[0039] 表 1
[0040]
[0042] 由表1得知，经本实用新型装置对某垃圾渗滤液污水处理24d后，污水中的化学需 氧量COD由419mg/L水质参数原样处理24d后，化学需氧量COD升至538mg/L。氨氮70mg/ L经处理24d后的升至83mg/L。系统中增加 UC模块反应器，可以有效地提高系统的可生化 性。
[0043] 如表2所示，为某污水处理厂使用本实用新型中HBF模块单元-(备用系统单元）， 在第1天至第24天的进水和出水数据对比情况。
[0047] 由表2得知，经本实用新型装置对某垃圾渗滤液污水处理24d后，污水中的化学需 氧量COD由538mg/L水质参数原样处理24d后，化学需氧量COD降至138mg/L。氨氮83mg/ L经处理24d后的降解6mg/L。HBF模块反应器可以加强脱氮效果。
[0048] 如表3所示，为某污水处理厂使用本实用新型对污水进行循环处理，COD去除率和 氨氮去除率情况。
[0052] 由表3得知，经本实用新型装置对污水处理24d后，污水COD去除率为67. 06% ;
[0053] 污水氨氮去除率为91. 43%。可以得知本实用新型具有良好的脱氮和去除化学需 氧量COD的效果。
[0054] 本实用新型的系统，流程简单，灵活，配水均匀，具有良好的微生物、污水反应体 系，处理效果更高效，而且投资省，自动化程度高。
[0055] 相对于现有技术，本实用新型具有如下优点：
[0056] (1)适用于高盐分废水：经过调试后整个系统中，生物相中的活性污泥和生物膜， 能搞适应含高盐分的工业废水，NaCl含量可达到lOOOOmg/L至12000mg/L，而Na2SO4含量可 达到 8000mg/L 至 10000mg/L。
[0057] (2)适用于低C/N比废水：系统中增加 UC模块反应器，可以有效地提高系统的可 生化性，而HBF模块反应器可以加强脱氮效果。因此，常规脱氮系统只有在C/N多4:1才会 对NH 3-N有较好的去除效果；本系统工艺对于4:1多C/N多2:1，也有极佳的效果。当系统 BOD浓度约为130mg/L，出水NH3-N浓度小于10mg/L。
[0058] 尽管本文较多地使用了点对点布水器1、上流式水解酸化池2、气浮池3、前置缺氧 池4、好氧池5、后置缺氧池6、第一序批式沉淀池7、第二序批式沉淀池8、中间水池9、过滤 器10、清水池11、达标水排放口 12、浓缩池13、脱水机14、干污泥外运口 15、污泥浓缩单元 16、UC模块单元17、HBF模块单元18、备用系统单元19、排放系统20等术语，但并不排除使 用其它术语的可能性。使用这些术语仅仅是为了更方便地描述和解释本实用新型的本质； 把它们解释成任何一种附加的限制都是与本实用新型精神相违背的。
[0059] 以上显示和描述了本实用新型的基本原理、主要特征和本实用新型的优点。本行 业的技术人员应该了解，本实用新型不受上述实施例的限制，上述实施例和说明书中描述 的只是说明本实用新型的原理，在不脱离本实用新型精神和范围的前提下，本实用新型还 会有各种变化和改进，本实用新型要求保护范围由所附的权利要求书、说明书及其等效物 界定。
Claims (7)
1. 一种高盐分低碳氮比化工废水的脱氮系统，其特征在于：包括UC模块单元（17)、气 浮池（3)、HBF模块单元（18)、备用系统单元（19)和排放系统（20)，所述UC模块单元（17)、 气浮池（3)、HBF模块单元（18)、备用系统单元（19)和排放系统（20)依次相连接；所述UC 模块单元（17)、HBF模块单元（18)和备用系统单元（19)分别与污泥浓缩单元（16)相连 接。
2. 根据权利要求1所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述UC 模块单元（17)包括依次相连接的点对点布水器（1)和上流式水解酸化池（2);所述点对点 布水器（1)和上流式水解酸化池（2)分别与气浮池（3)相连接； 所述HBF模块单元（18)包括污水栗、前置缺氧池（4)、好氧池（5)、后置缺氧池（6)和 序批式沉淀池，所述前置缺氧池（4)、好氧池（5)、后置缺氧池（6)和序批式沉淀池依次相连 接； 所述备用系统单元（19)包括依次相连接的中间水池（9)、过滤器（10)和清水池（11); 所述污泥浓缩单元（16)包括依次相连接的浓缩池（13)和脱水机（14); 所述排放系统（20)包括干污泥外运口（15)和达标水排放口（12);所述污泥浓缩单元 (16)与干污泥外运口（15)相连接；所述备用系统单元（19)与达标水排放口（12)相连接。
3. 根据权利要求2所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述上 流式水解酸化池（2)设有36根配水软管，所述点对点布水器（1)通过配水软管和上流式水 解酸化池（2)底部相连接；所述上流式水解酸化池（2)从底部到上部依次设置有污泥床反 应区、稠合沉淀反应区和澄清区。
4. 根据权利要求2所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述好 氧池（5)内设置有溶氧仪；所述序批式沉淀池包括第一序批式沉淀池（7)和第二序批式沉 淀池（8); 所述第一序批式沉淀池（7)和第二序批式沉淀池（8)分别通过污水栗与后置缺氧池 (6)相连接。
5. 根据权利要求4所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述好 氧池（5)、第一序批式沉淀池（7)和第二序批式沉淀池（8)内分别设置有酶浮填料和曝气装 置； 所述曝气装置包括射流曝气器和射流循环栗，所述射流曝气器与射流循环栗相连接。
6. 根据权利要求2所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述过 滤器（10)为石英砂过滤器。
7. 根据权利要求2所述的高盐分低碳氮比化工废水的脱氮系统，其特征在于：所述浓 缩池（13)为重力浓缩池或气浮池；所述脱水机（14)为板框脱水机或带式脱水机。
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| CN110204057A (zh) * | 2019-06-20 | 2019-09-06 | 湖北中地星河环保科技有限公司 | 一种用耐高盐反硝化细菌处理高盐污水的工艺 |
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| CN105060654A (zh) * | 2015-09-02 | 2015-11-18 | 上海泓济环保工程有限公司 | 高盐分低碳氮比化工废水的脱氮系统及其处理方法 |
| CN110204057A (zh) * | 2019-06-20 | 2019-09-06 | 湖北中地星河环保科技有限公司 | 一种用耐高盐反硝化细菌处理高盐污水的工艺 |
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