CN207175699U - 一种用于厌氧处理造纸污水的分离器 - Google Patents
一种用于厌氧处理造纸污水的分离器 Download PDFInfo
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- CN207175699U CN207175699U CN201720881284.9U CN201720881284U CN207175699U CN 207175699 U CN207175699 U CN 207175699U CN 201720881284 U CN201720881284 U CN 201720881284U CN 207175699 U CN207175699 U CN 207175699U
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O=C1C=CC(=O)C=C1 AZQWKYJCGOJGHM-UHFFFAOYSA-N 0.000 description 1
- MWPLVEDNUUSJAV-UHFFFAOYSA-N Anthracene Chemical compound 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Abstract
本实用新型公开了一种用于厌氧处理造纸污水的分离器，设置规则且密集的注水口和导流板道，使分离器内液体流动均匀，且设置填料区，进一步地将固态杂质留在下方的污泥沉淀区，且对于分离器上部进行机械搅拌和设置侧壁的溢水槽，使气体充分排出，液体经充分搅拌过滤后溢出，保证了固液气三相分离的分离效果，促进了后续厌氧污水处理的处理效果；使用新型凝胶球型填料，颗粒多且多孔，其比表面积大，能够对分离液体充分吸附、过滤，使分离器能够将填料上的生物保留在反应区内，从而进一步的降低了污泥出水COD，减少了好氧系统负荷和污泥生长量，本实用新型适用于用于厌氧处理造纸污水的分离器。
Description
一种用于厌氧处理造纸污水的分离器
技术领域
[0001]本实用新型涉及一种用于厌氧处理造纸污水的分离器领域，特别涉及一种用于厌 氧处理造纸污水的分离器。
背景技术
[0002]制浆造纸污水属于高色度、高碱度、高有机污染物、可生化降解性低的高难度工 业废水。污水来源于备料、蒸煮、漂白、造纸等工段，污水中含有多种烷、烃、酚、酸、苯、醇、 醛、酮、醚、蒽、醌、糖、胺、纤维素、半纤维素和木素等有机物及其衍生物、聚合物、卤代物。 制浆造纸企业在进行碱回收后，通常采用常规的厌氧加好氧处理工艺，在设计合理与污水 处理设施运行较好的情况下，其出水基本能GB3544-2001标准的要求，但无法满足新的国 家标准《制浆造纸工业水污染物排放标准》GB3544-2008的要求，所以在二级生化处理后进 行深度处理，造成了处理流程长、建造成本高、运行费用高的特点。
[0003]制浆造纸污水深度处理工艺即为在厌氧状态下，污水中的有机物被厌氧细菌分 解、代谢、消化，使得污水中的有机物含量大幅减少，同时产生沼气的一种高效的污水处理 方式。污水中的机物污染程度一般用化学需氧量COD来作为指标，降低厌氧处理后污水的 COD是改进厌氧深度处理污水技术的主要目标。在采用UASB (上流式厌氧污泥床反应器)厌 氧生物方法处理污水时，UASB由污泥反应区、气液固三相分离器(包括沉淀区）和集气室三 部分组成，其中三相分离器由沉淀区、回流缝和气封组成，其功能是将气体(沼气）、固体(污 泥)和液体(废水)等三相进行分离，沼气进入气室，污泥在沉淀区进行沉淀，并经回流缝回 流到反应区，三相分离器的分离效果将直接影响反应器的处理效果。
[0004] 如公告号为中国专利CN201473389,公开了一种上流式厌氧污泥反应器，能够将生 物气带出的污泥通过回流管回流到反应器底部，并与进水充分混合，大大提高了废水处理 的效果，但是无法去除废水中无法参与反应的部分有机污染物，也难以除尽废水中残余的 微小气泡，三相分离的效果欠佳。 实用新型内容
[0005]为了克服上述现有技术的不足，本实用新型提供了一种用于厌氧处理造纸污水的 分离器，三相分离效果好，采用出水截留，能将填料上的生物保留在反应区，进一步降低了 厌氧出水C0D。
[0006]为达到上述目的，本实用新型解决其技术问题所采用的技术方案是:一种用于厌 氧处理造纸污水的分离器，包括由下至上的污泥沉淀区、注水区、填料区、导流区，搅拌区、 出气口和搅拌动力机构，所述污泥沉淀区呈倒圆台状，所述注水区包括接通器壁的进水管 道、内部通水的分水板框，所述分水板框包括分水管道网和位于分水管道网各节点处的注 水口，所述填料区的底部对应器壁设有进液口，所述填料区包括若干层填料块，所述填料块 内装填有凝胶颗粒，所述凝胶颗粒呈球体、且其表面均匀密布有微观圆孔，所述导流区包括 竖直设置的若干导流板道，所述搅拌区包括搅拌轴、搅拌叶和搅拌刮板，所述搅拌叶呈双螺 带状，围绕所述搅拌区的器壁设有滤网，所述滤网的外侧环绕设有溢水槽，所述溢水槽的底 部设有往上倾斜45度的溢水底板，所述溢水槽的槽口高出滤网顶部。
[0007]作为优选，所述进液口连接有污水储池，所述进液口与污水储池间设有流量阀。 [0008]作为优选，所述污泥沉淀区的底部连通有污泥沉淀池。
[0009]作为优选，所述进水管道连接有储水池，所述进水管道和储水池间设有抽水泵。 [0010]作为优选，所述溢水槽外对应设有收集溢出水的处理水收集池。
[0011] 作为优选，所述出气口的数目为2个，一对所述出气口均连通集气室。
[0012]由于上述技术方案的运用，本实用新型与现有技术相比具有下列有益效果：
[0013] 1 •设置规则且密集的注水口和导流板道，使分离器内液体流动均匀，且设置填料 区，进一步地将固态杂质留在下方的污泥沉淀区，且对于分离器上部进行机械搅拌和设置 侧壁的溢水槽，使气体充分排出，液体经充分搅拌过滤后溢出，保证了固液气三相分离的分 离效果，促进了后续厌氧污水处理的处理效果；
[0014] 2•使用新型凝胶球型填料，颗粒多且多孔，其比表面积大，能够对分离液体充分吸 附、过滤，使分离器能够将填料上的生物保留在反应区内，从而进一步的降低了污泥出水 COD，减少了好氧系统负荷和污泥生长量。
附图说明
[0015]图1是本实施例的结构示意图。
[0016]图2是本实施例中分水板框的俯视图。
[0017]图3是本实施例中凝胶颗粒表面的微观示意图。
[0018]图4是本实施例的连接关系示意图。
[0019]图中：1、污泥沉淀区；2、注水区；21、进水管道；22、分水板框；221、分水管道网； 222、注水口； 3、填料区；31、进液口； 32、填料块;321、凝胶颗粒;3211、微观圆孔;4、导流区； 41、导流板道;5、搅拌区;51、搅拌轴;52、搅拌叶;53、搅拌刮板;54、滤网;55、溢水槽;551、溢 水底板;6、出气口； 7、搅拌动力机构;8、污水储池;81、流量阀；9、污泥沉淀池；10、储水池； 11、抽水栗;12、处理水收集池;13、集气室。
具体实施方式
[0020] 下面结合具体实施例，对本实用新型的内容做进一步的详细说明：
[0021] 如图1所示，本实施例是用于厌氧工艺处理造纸污水的一种固液气三相分离器，整 体上呈底部收束为倒圆台的圆柱体，包括由下至上的污泥沉淀区1、注水区2、填料区3、导流 区4，搅拌区5、出气口 6和搅拌动力机构7，污泥沉淀区1呈倒圆台状，注水区2包括接通器壁 的进水管道21、内部通水的分水板框22,填料区3的底部对应器壁设有进液口 31，填料区3包 括若干层填料块32,导流区4包括竖直设置的若干导流板道41，搅拌区5包括搅拌轴51、搅拌 叶52和搅拌刮板53，搅拌叶52呈双螺带状，竖直的搅拌刮板53连接搅拌叶52的端头，搅拌刮 板53与滤网54间留有间隙，围绕搅拌区5的器壁设有滤网54,滤网54的外侧环绕设有溢水槽 55，溢水槽55的底部设有往上倾斜45度的溢水底板551，溢水槽55的槽口高出滤网54顶部。 [0022]如图2所示，填料块32内装填有凝胶颗粒321，凝胶颗粒321呈球体、且其表面均匀 密布有微观圆孔3211，凝胶颗粒321的直径为〇.8cm〜lcm，因其颗粒小且表面微观多孔，故比 表面面积大，吸附能力强，能够留住部分大分子的有机污染物和其他杂质。
[0023]如图3所示，分水板框22包括分水管道网221和位于分水管道网221各节点处的注 水口 222，在本实施例中分水管道网221呈正方形栅格状，包括32个节点即32个出水口，出水 口呈圆形，使污水和注水混合均匀，污水溶液均匀流动、过滤分离，降低液体中的含泥率和 其他杂质的含量，从而改善出液的水质。
[0024]结合图1和图4，进液口 31连接有污水储池8，进液口 31与污水储池8间设有流量阀 81，污泥沉淀区1的底部连通有污泥沉淀池9，污泥沉淀池9内的高浓度污泥床污泥浓度可达 6〇_8〇g/L，进水管道21连接有储水池10,进水管道21和储水池10间设有抽水泵11，溢水槽55 外对应设有收集溢出水的处理水收集池12，出气口 6的数目为2个，一对出气口 6均连通集气 室I3，本分离器是UASB中的一环，它用装有凝胶颗粒3M的填料将污水中的部分有机物吸收 截留，并将污水分离为固态的污泥、液态的处理水、气态的废气，故分离器表壁各进出管口 连接USAB中其他反应设施。
[0025]本实施例的工作原理是:将含有废气、污泥的污水从污水储池8通入分离器内，并 以流量阀81控制流量，同时储水池10通过抽水栗11给反应器注水，多个均布的注水口 222出 水混合稀释进入污水并形成水流，具有良好的沉淀性能和凝聚性能的污泥在下部的污泥沉 淀区1汇集，沿倾斜的器壁不断累积后进入污泥沉淀池9，分离器内液体逐渐上升经过填料 区3吸附截留部分有机污染物，再通过导流板道41进入搅拌区5，液体内气体从上方的出气 口6排出进入集气室I3,处理水穿过侧壁的滤网54,从溢水槽55的上端溢出进入处理水收集 池12,完成三相分离。
[0026]本实施例的有益效果是:设置规则且密集的注水口 222和导流板道41，使分离器内 液体流动均匀，且设置填料区3，进一步地将固态杂质留在下方的污泥沉淀区丨，且对于分离 器上部进行机械搅拌和设置侧壁的溢水槽55,使气体充分排出，液体经充分搅拌过滤后溢 出，保证了固液气三相分离的分离效果，促进了后续厌氧污水处理的处理效果;使用新型凝 胶球型填料，颗粒多且多孔，其比表面积大，能够对分离液体充分吸附、过滤，使分离器能够 将填料上的生物保留在反应区内，从而进一步的降低了污泥出水C0D，减少了好氧系统负荷 和污泥生长量。
[0027]上述实施例只为说明本实用新型的技术构思及特点，其目的在于让熟悉此项技术 的人士能够了解本实用新型的内容并加以实施，并不能以此限制本实用新型的保护范围， 凡根据本实用新型精神实质所作的等效变化或修饰，都应涵盖在本实用新型的保护范围 内。
Claims (6)
1.一种用于厌氧处理造纸污水的分离器，其特征在于：包括由下至上的污泥沉淀区 ⑴、注水区（2)、填料区⑶、导流区⑷，搅拌区⑸、出气口⑹和搅拌动力机构⑺，所述污 泥沉淀区（1)呈倒圆台状，所述注水区（2)包括接通器壁的进水管道(21)、内部通水的分水 板框(2¾，所述分水板框(22)包括分水管道网（221)和位于分水管道网（221)各节点处的注 水口（222)，所述填料区⑶的底部对应器壁设有进液口（31)，所述填料区⑶包括若干层填 料块(32)，所述填料块(32)内装填有凝胶颗粒(Ml)，所述凝胶颗粒(321)呈球体、且其表面 均匀密布有微观圆孔(3211)，所述导流区⑷包括竖直设置的若干导流板道(41)，所述搅拌 区（5)包括搅拌轴(51)、搅拌叶(5¾和搅拌刮板(M)，所述搅拌叶(52)呈双螺带状，围绕所 述搅拌区(5)的器壁设有滤网（54)，所述滤网¢4)的外侧环绕设有溢水槽(55)，所述溢水槽 (55)的底部设有往上倾斜45度的溢水底板(551)，所述溢水槽(55)的槽口高出滤网（54)顶 部。
2.根据权利要求1所述的一种用于厌氧处理造纸污水的分离器，其特征在于:所述进液 口（31)连接有污水储池(8)，所述进液口（31)与污水储池⑻间设有流量阀(81)。
3.根据权利要求1所述的一种用于厌氧处理造纸污水的分离器，其特征在于:所述污泥 沉淀区⑴的底部连通有污泥沉淀池(9)。
4.根据权利要求1所述的一种用于厌氧处理造纸污水的分离器，其特征在于:所述进水 管道(21)连接有储水池(1〇)，所述进水管道(2丨)和储水池(1〇)间设有抽水栗(n)。
5.根据权利要求1所述的一种用于厌氧处理造纸污水的分离器，其特征在于:所述溢水 槽(55)外对应设有收集溢出水的处理水收集池(1¾。 八 ‘
6.根据权利要求1所述的一种用于厌氧处理造纸污水的分离器，其特征在于:所述出气 口⑹的数目为2个，一对所述出气口⑹均连通集气室(1¾。
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