CN210825844U - 一种复合型污水处理*** - Google Patents
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Abstract
本实用新型公开了一种复合型污水处理***，包括预处理单元、地下渗滤单元和生态处理单元，所述预处理单元、地下渗滤单元和生态处理单元横向依次排布连接，地下渗滤单元包括覆盖层、好氧层、厌氧层和深度除磷层，覆盖层、好氧层、厌氧层和深度除磷层从上至下依次排列，好氧层、厌氧层和深度除磷层的体积比为2:1.5:1‑3:2:1。有益效果：整套设施可埋于地下，占地小、运行成本低、维护管理简便、使用灵活；地下渗滤单元中的高效好氧、厌氧微生物菌剂，可以更加有效的分解转化污水中的有机物，深度除磷层将污水中的磷转化为磷酸盐，再经生态处理单元进一步去除各种污染物，通过地下渗滤单元和生态处理单元的配合使用，使排放出的水质更好，更有益于环境保护。
Description
技术领域
本实用新型涉及污水处理技术领域，具体涉及一种复合型污水处理***。
背景技术
随着农村经济的发展，农村地区生活水平不断提高，农村生活污水的排放量也不断增加，在国家对生态环境的重视下，农村污水处理越来越受到各省市的重视。污水处理的技术很多，主要有生物处理技术(接触氧化、SBR)、人工湿地技术和传统地下渗滤技术，但生物处理技术运行费用高且维护管理复杂，传统地下渗滤技术和人工湿地技术占地面积大、造价成本高，人工湿地运行受气候条件限制且容易滋生蚊虫，传统地下渗滤技术中的结构层比较繁杂，排出水的水质不好。因此需为国内农村的污水治理提供更加环保、经济、稳定和可行的***解决方案，解决村镇生活污水的污染问题。
实用新型内容
本实用新型的目的克服现有技术的不足，提供一种更加经济、环保、更具实用性的复合型污水处理***。
本实用新型的目的是通过以下技术措施达到的：
一种复合型污水处理***，包括预处理单元、地下渗滤单元和生态处理单元，所述预处理单元、地下渗滤单元和生态处理单元横向依次排布连接，所述生态处理单元包括覆盖层和生态层，所述地下渗滤单元包括覆盖层、好氧层、厌氧层和深度除磷层，所述覆盖层、好氧层、厌氧层和深度除磷层从上至下依次排列，好氧层、厌氧层和深度除磷层的体积比为2:1.5:1-3:2:1。
进一步地：所述好氧层包括人工滤料或天然滤料和高效好氧微生物菌剂，人工滤料或天然滤料和高效好氧微生物菌剂的体积比为6:1-8:1。
进一步地：所述厌氧层包括人工滤料或天然滤料和高效厌氧微生物菌剂，人工滤料或天然滤料和高效厌氧微生物菌剂的体积比为6:1-8:1。
进一步地：所述天然滤料包括但不限于细砂、砾石、灰渣、碎石、鹅卵石、天然沸石。
进一步地：所述人工滤料包括但不限于石英砂、陶粒、人工沸石、粉煤灰。
进一步地：所述好氧层和厌氧层的厚度均为0.1m-0.3m。
进一步地：所述的深度除磷层包括岩石矿物材料和固液分离材料，深度除磷层的厚度为0.1m-0.3m。
进一步地：所述固液分离材料包括植物枝叶、谷皮、根和天然土的一种或者多种。
进一步地：所述预处理单元包括格栅池、沉淀池、厌氧池和调节池，所述格栅池、沉淀池、厌氧池和调节池水平横向依次排布，所述调节池内置有提升泵。
进一步地：所述厌氧池内填充有弹性生物材料，弹性生物材料上设有生物膜。
与现有技术相比，本实用新型的有益效果是：1.整套设施可以全埋于地下，占地小且不需要专用土地、投资小、运行成本低、维护管理简便、运行稳定、使用灵活；2.地下渗滤单元中的高效微生物菌剂，可以更加有效的分解转化污水中的有机物，深度除磷层将污水中的磷转化为磷酸盐，再经生态处理单元进一步去除各种污染物，通过地下渗滤单元和生态处理单元的相互配合使用，能够使排放出的水质更好、更优，更加有益于环境保护。
下面结合附图和具体实施方式对本实用新型作详细说明。
附图说明
图1是本实用新型的结构示意图。
其中，1.格栅池，2.沉淀池，3.厌氧池，4.弹性生物材料，5.调节池，6.提升泵，7.地下渗滤单元，8.好氧层，9.厌氧层，10.深度除磷层，11.生态层，12.生态处理单元，13.覆盖层，14.预处理单元。
具体实施方式
实施例，如图1所示，一种复合型污水处理***，包括预处理单元14、地下渗滤单元7和生态处理单元12，所述预处理单元14、地下渗滤单元7和生态处理单元12横向依次排布连接，将预处理单元14、地下渗滤单元7和生态处理单元12有机结合，使污染物在各单元之间自动调节分配，保障***的长期稳定运行，所述生态处理单元12包括覆盖层13和生态层11，所述地下渗滤单元7包括覆盖层13、好氧层8、厌氧层9和深度除磷层10，所述覆盖层13、好氧层8、厌氧层9和深度除磷层10从上至下依次排列，好氧层8、厌氧层9和深度除磷层10的体积比为2:1.5:1-3:2:1，整套设施可以全埋于地下，占地小且不需要专用土地、投资小、运行成本低、维护管理简便、运行稳定、使用灵活。
所述好氧层8包括人工滤料或天然滤料和高效好氧微生物菌剂，人工滤料或天然滤料和高效好氧微生物菌剂的体积比为6:1-8:1。
所述厌氧层9包括人工滤料或天然滤料和高效厌氧微生物菌剂，人工滤料或天然滤料和高效厌氧微生物菌剂的体积比为6:1-8:1。
好氧层8和厌氧层9中的高效好氧微生物菌剂和高效厌氧微生物菌剂，可以更加有效的分解转化污水中的有机物，进一步提升排出水的水质。
所述天然滤料包括但不限于细砂、砾石、灰渣、碎石、鹅卵石、天然沸石。
所述人工滤料包括但不限于石英砂、陶粒、人工沸石、粉煤灰。
所述好氧层8和厌氧层9的厚度均为0.1-0.3m。
所述的深度除磷层10包括岩石矿物材料和固液分离材料，深度除磷层10的厚度为0.1m-0.3m。
所述固液分离材料包括植物枝叶、谷皮、根和天然土的一种或者多种。
污水中的磷颗粒通过与岩石矿物材料中的Fe，Al，Ca，Mg等金属阳离子发生化学沉淀作用，形成不溶性磷酸盐沉淀，然后通过固液分离将磷从污水中除去，最终以磷酸盐矿物形式富集，再经生态处理单元12进一步处理后达标排放。
所述预处理单元14包括格栅池1、沉淀池2、厌氧池3和调节池5，所述格栅池1、沉淀池2、厌氧池3和调节池5水平横向依次排布，所述调节池5内置有提升泵6，污水有序的依次经过格栅池1、沉淀池2和厌氧池3，先过滤分解部分污染物，再流入调节池5，在调节池5内提升泵6的作用下，污水进入地下渗滤单元7。
所述厌氧池3内填充有弹性生物材料4，弹性生物材料4上设有生物膜，膜上微生物通过生物絮凝、吸附、氧化等作用降解原水中的污染物。
表1复合型污水处理***处理污水实验数据
| 序号 | 地下渗滤***进水(mg/L) | 地下渗滤***出水(mg/L) |
| 1 | 278 | 46 |
| 2 | 250 | 35 |
| 3 | 320 | 48 |
利用本处理***对污水进行处理，达到城镇污水处理厂污染物排放一级A标准，该处理过程如下：
实施例1
污水经预处理单元14横向运移清除部分污染物，在提升泵6的作用下，经过预先处理的污水进入地下渗滤单元7，好氧层8、厌氧层9和深度除磷层10的体积比为2:1.5:1，好氧层8厚度为0.3m且好氧层8中滤料(使用天然滤料：细砂、砾石、灰渣、碎石)和高效好氧微生物菌剂的体积比为6:1，厌氧层9厚度为0.3m且厌氧层9中滤料(使用天然滤料：鹅卵石、天然沸石)和高效厌氧微生物菌剂的体积比为6:1，深度除磷层10的厚度为0.3m且深度除磷层10的固液分离材料为植物枝叶，污水在地下渗滤单元7的好氧层8、厌氧层9及深度除磷层10中竖向渗滤，其中的污染物被各个功能结构层的滤料拦截、吸附，并通过微生物分解转化，最终进入到生态处理单元12，在生态处理单元12的过滤、吸附、沉淀、离子交换、植物吸收和微生物分解等作用下得到进一步净化，达到《城镇污水处理厂污染物排放标准GB18918－2002》表1一级A的标准被排出。
实施例2
污水经预处理单元14横向运移清除部分污染物，在提升泵6的作用下，经过预先处理的污水进入地下渗滤单元7，好氧层8、厌氧层9和深度除磷层10的体积比为2.5:1.5:1，好氧层8厚度为0.2m且好氧层8中滤料(使用人工滤料：石英砂、陶粒)和高效好氧微生物菌剂的体积比为7:1，厌氧层9厚度为0.2m且厌氧层9中滤料(使用人工滤料：人工沸石、粉煤灰)和高效厌氧微生物菌剂的体积比为7:1，深度除磷层10的厚度为0.2m且深度除磷层10的固液分离材料为植物枝叶和谷皮，污水在地下渗滤单元7的好氧层8、厌氧层9及深度除磷层10中竖向渗滤，其中的污染物被各个功能结构层的滤料拦截、吸附，并通过微生物分解转化，最终进入到生态处理单元12，在生态处理单元12的过滤、吸附、沉淀、离子交换、植物吸收和微生物分解等作用下得到进一步净化，达到《城镇污水处理厂污染物排放标准GB18918－2002》表1一级A的标准被排出。
实施例3
污水经预处理单元14横向运移清除部分污染物，在提升泵6的作用下，经过预先处理的污水进入地下渗滤单元7的好氧层8、厌氧层9和深度除磷层10的体积比为3:2:1，好氧层8厚度为0.1m且好氧层8中滤料(使用天然滤料：鹅卵石、天然沸石)和高效好氧微生物菌剂的体积比为8:1，厌氧层9厚度为0.1m且厌氧层9中滤料(使用人工滤料：石英砂和陶粒)和高效厌氧微生物菌剂的体积比为8:1，深度除磷层10的厚度为0.1m且深度除磷层10的固液分离材料为根、谷皮和天然土，污水在地下渗滤单元7的好氧层8、厌氧层9及深度除磷层10中竖向渗滤，其中的污染物被各个功能结构层的滤料拦截、吸附，并通过微生物分解转化，最终进入到生态处理单元12，在生态处理单元12的过滤、吸附、沉淀、离子交换、植物吸收和微生物分解等作用下得到进一步净化，达到《城镇污水处理厂污染物排放标准GB18918－2002》表1一级A的标准被排出。
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，这些变化和改进都落入要求保护的本实用新型范围内。本实用新型要求保护范围由所附的权利要求书及其等效物界定。
Claims (10)
1.一种复合型污水处理***，包括预处理单元、地下渗滤单元和生态处理单元，所述预处理单元、地下渗滤单元和生态处理单元横向依次排布连接，所述生态处理单元包括覆盖层和生态层，其特征在于：所述地下渗滤单元包括覆盖层、好氧层、厌氧层和深度除磷层，所述覆盖层、好氧层、厌氧层和深度除磷层从上至下依次排列，好氧层、厌氧层和深度除磷层的体积比为2:1.5:1-3:2:1。
2.根据权利要求1所述的复合型污水处理***，其特征在于：所述好氧层包括人工滤料或天然滤料和高效好氧微生物菌剂，人工滤料或天然滤料和高效好氧微生物菌剂的体积比为6:1-8:1。
3.根据权利要求1所述的复合型污水处理***，其特征在于：所述厌氧层包括人工滤料或天然滤料和高效厌氧微生物菌剂，人工滤料或天然滤料和高效厌氧微生物菌剂的体积比为6:1-8:1。
4.根据权利要求2或3所述的复合型污水处理***，其特征在于：所述天然滤料包括但不限于细砂、砾石、灰渣、碎石、鹅卵石、天然沸石中的一种或几种。
5.根据权利要求2或3所述的复合型污水处理***，其特征在于：所述人工滤料包括但不限于石英砂、陶粒、人工沸石、粉煤灰中的一种或几种。
6.根据权利要求1所述的复合型污水处理***，其特征在于：所述好氧层和厌氧层的厚度均为0.1-0.3m。
7.根据权利要求1所述的复合型污水处理***，其特征在于：所述的深度除磷层包括岩石矿物材料和固液分离材料，深度除磷层的厚度为0.1m-0.3m。
8.根据权利要求7所述的复合型污水处理***，其特征在于：所述固液分离材料包括植物枝叶、谷皮、根和天然土的一种或者多种。
9.根据权利要求1所述的复合型污水处理***，其特征在于：所述预处理单元包括格栅池、沉淀池、厌氧池和调节池，所述格栅池、沉淀池、厌氧池和调节池水平横向依次排布，所述调节池内置有提升泵。
10.根据权利要求9所述的复合型污水处理***，其特征在于：所述厌氧池内填充有弹性生物材料，弹性生物材料上设有生物膜。
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