CN209065651U - 卫生间粪尿资源化处理设备 - Google Patents
卫生间粪尿资源化处理设备 Download PDFInfo
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- CN209065651U CN209065651U CN201821042647.0U CN201821042647U CN209065651U CN 209065651 U CN209065651 U CN 209065651U CN 201821042647 U CN201821042647 U CN 201821042647U CN 209065651 U CN209065651 U CN 209065651U
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- fecaluria
- pipe
- toilet
- pump
- sludge
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- 206010059410 Faecaluria Diseases 0.000 title claims abstract description 91
- 238000004064 recycling Methods 0.000 title claims abstract description 19
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- 244000052616 bacterial pathogens Species 0.000 claims abstract description 6
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- 238000000354 decomposition reaction Methods 0.000 claims description 16
- 238000000926 separation method Methods 0.000 claims description 15
- CBENFWSGALASAD-UHFFFAOYSA-N ozone Chemical compound 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- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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Abstract
一种卫生间粪尿资源化处理设备，包括粪便分解系统、微生物处理系统和高级氧化系统，本实用新型不仅有效解决了粪尿污水直接排入下水管道，导致水资源的浪费和环境污染的问题，而且有效解决了现有卫生间的废水回用问题及卫生间臭味问题。
Description
技术领域
本实用新型涉及卫生间粪尿，特别是一种卫生间粪尿资源化处理设备。
背景技术
卫生间的粪尿是城市生活污水的主要污染源之一，卫生间尤其是移动卫生间的粪尿为高浓度有机物污水，它的化学需氧量(COD)、氨氮、生化需氧量(BOD)、悬浮物含量(SS)等指标远远高于城市污水。城市生活用水中掺杂了洗澡水、洗衣水等等，稀释了粪尿的有机物含量，进水的化学需氧量COD<400mg/L、氨氮<30mg/L、生化需氧量BOD>200mg/L、悬浮物含量SS<200mg/L；厕所污水与单纯的生活污水有以下不同，污染指标高；单纯的粪便污水的污染指标一般的化学需氧量CODcr17000-30000mg/L，氨氮在7000-11000mg/L之间，甚至更高；进水水质波动较大，如厕人员的大小便比例无规律可循，进水水量变化不定；如厕人数的多少随季节、天气、节假日的变化而变化，并且无任何规律可循。
鉴于厕所污水的以上特点，利用传统的污水处理工艺不可能有好的处理效果。特殊的污水必须以特殊处理工艺，才能达到出水标准。
目前，城市移动卫生间及旅游景点卫生间的粪尿处理主要技术是：
1、粪尿分离后固体进入微生物床进行分解，液体进入城市污水管道；
2、粪尿直接进入化粪池，排入附近的河道和市政管网；
3、粪尿分离后固体进入微生物床进行分解，液体通过初步消毒、杀菌后进行冲厕；
4、打包式收集便器；
5、泡沫封堵式便器等等。
现阶段城市生活污水及新农村改造的污水处理主要为微生物技术进行分解和发酵，如日本净化槽技术适用于低浓度的有机污水及对水质要求较高和经济较发达地区选用，对于中高浓度的有机污水及我国中西部地区，尚没有使用净化槽处理分散污水的报道。随着国家对污水排放的重视，单一的处理技术已经不能满足国家污水排放的要求。
实用新型内容
本实用新型提供一种卫生间粪尿资源化处理设备，该设备结合了化粪池分解、微生物处理及高级氧化技术。克服了现有卫生间粪尿处理技术的不足，从源头对高浓度粪尿进行固液分离，降解化学需氧量COD、氨氮、生化需氧量BOD、悬浮物含量SS等有机物，通过光催化氧化的深度处理，进一步对粪尿污水进行净化，杀菌、消毒、脱色处理，使回用的冲厕水具有消毒、除臭功能，切断了污水中病毒，保证了卫生间的清洁，减少了卫生间的臭味。能实现卫生间粪尿污水零排放和资源再生利用，有效地避免了传统处理方法污泥和沉淀物产生的新污染问题。
本实用新型的技术解决方案如下：
一种卫生间粪尿资源化处理设备，其特点在于包括粪便分解系统、微生物处理系统和高级氧化系统：
所述的粪便分解系统包括固液分离器、收集桶、粪便分解反应器,所述的固液分离器包含粪尿管、分离板、污泥泵、送粪管、粪尿回流管、自流液管；所述的收集桶包含粪尿回流泵、过滤网、固体物收集桶；所述的粪便分解反应器包含单向阀、液位传感器、粪尿输出泵、分解微生物床、污泥泵、污泥输送管和粪尿输出管；
所述的微生物处理系统包括厌氧池、好氧池、MBR反应器；所述的厌氧池包括厌氧池生物膜、厌氧池排污泵、厌氧自流管；所述的好氧池包含好氧池生物膜、好氧池污泥输送泵、好氧曝气管、高压风机；所述的MBR反应器包括MBR反应器输送管、MBR自吸泵；
所述的高级氧化系统包括光催化厌氧反应器、回用水箱；所述的光催化氧化反应器包含紫外线灯、臭氧曝气头、臭氧管、氧气源臭氧发生器；所述的回用水箱包含回用水输入管、回用水输出管；
所述的卫生间便器的粪尿经粪尿管进入所述的固液分离器，粪尿经所述的分离板进行初步分离，固体粪便和卫生纸由送粪管进入固体物收集桶，固体物通过过滤网进行第二次过滤，过滤后的粪尿液体进入所述的收集桶，由所述的粪尿输送泵驱动经所述的粪尿回流管回流到所述的固液分离器进行再分离；分离后的液体粪尿通过自流液管进入所述的粪便分解反应器的下端，再通过分解微生物床的分解、过滤后的液体上升到控制液位，液位传感器触发，粪尿输送泵驱动所述的粪尿经所述的粪尿输送管进入厌氧池，所述的粪尿输送管安装有单向阀，防止厌氧池的粪尿液体回流，固液分离器内的污泥泵和粪便分解反应器的污泥泵定期抽吸污泥，通过污泥输送管送入所述的固体物收集桶，通过过滤网进行固液分离，分离后的液体通过粪尿回流泵再送入固液分离器；
经所述的粪尿输送管进入厌氧池的粪尿，通过和所述的厌氧池生物膜的反应，反应时间为20小时，粪尿经厌氧池分解部分有机物，上清液通过厌氧自流管进入所述的好氧池，通过好氧池生物膜以及由高压风机对好氧池曝气管的曝气，保证了微生物的溶解氧，进一步降解粪尿有机物，反应时间20小时，粪尿污水进入所述的MBR反应器，通过MBR自吸泵及MBR反应器输送管把经所述的好氧池生物膜分离后的上清液送入所述的光催化氧化反应器内，上清液通过紫外线灯和臭氧曝气头输出的臭氧进行有机物降解、消毒、杀菌、脱色；臭氧曝气头的臭氧由氧气源臭氧发生器通过臭氧管供应；处理好的上清液通过所述的回用水输入管进入回用水箱，回用水通过回用水输出管进入卫生间冲洗或绿化浇灌,所述的厌氧池排污泵和所述的好氧池污泥输送泵也定期抽吸污泥，通过污泥输送管送入所述的固体物收集桶。
本实用新型的技术效果：
本实用新型不仅有效地解决了粪尿污水直接排入下水管道，导致水资源的浪费和污染问题，而且有效地解决了现有卫生间的废水回用问题及卫生间臭味问题，处理后的回用水达到了《城市污水再生利用、城市杂水水质》(GB/T18920-2002)中城市杂用水类标准。
附图说明
图1为本实用新型卫生间粪尿资源化处理设备的结构示意图。
具体实施方式
请参阅图1，图1为本实用新型卫生间粪尿资源化处理设备的结构示意图。由图可见，本实用新型卫生间粪尿资源化处理设备，包括粪便分解系统、微生物处理系统和高级氧化系统：
所述的粪便分解系统包括固液分离器108、收集桶106、粪便分解反应器112,所述的固液分离器108包含粪尿管100、分离板101、污泥泵102、送粪管103、粪尿回流管104、自流液管109；所述的收集桶106包含粪尿回流泵105、过滤网107、固体物收集桶117；所述的粪便分解反应器112包含单向阀110、液位传感器111、粪尿输出泵113、分解微生物床114、污泥泵115、污泥输送管116、粪尿输出管118；
所述的微生物处理系统包括厌氧池20、好氧池207、MBR反应器208；所述的厌氧池200包括厌氧池生物膜201、厌氧池排污泵202、厌氧自流管203；所述的好氧池207包含好氧池生物膜204、好氧池污泥输送泵205、好氧曝气管206、高压风机211；所述的MBR反应器208包括MBR反应器输送管209和MBR自吸泵210；
所述的高级氧化系统包括光催化厌氧反应器300、回用水箱306；所述的光催化氧化反应器300包含紫外线灯301、臭氧曝气头302、臭氧管305、氧气源臭氧发生器307；所述的回用水箱306包含回用水输入管303、回用水输出管304；
所述的卫生间便器的粪尿经粪尿管100进入所述的固液分离器108，粪尿经所述的分离板101进行初步分离，固体粪便和卫生纸由送粪管103进入固体物收集桶117，固体物通过过滤网107进行第二次过滤，过滤后的粪尿液体进入所述的收集桶106，粪尿液体由所述的粪尿输送泵105驱动经所述的粪尿回流管104回流到所述的固液分离器108进行再分离；分离后的液体粪尿通过自流液管109进入所述的粪便分解反应器112的下端，再通过分解微生物床114的分解、过滤后的液体上升到控制液位，液位传感器111触发，粪尿输送泵113驱动所述的粪尿经所述的粪尿输送管118进入厌氧池200，所述的粪尿输送管118安装有单向阀110，防止厌氧池200的粪尿液体回流，固液分离器108内的污泥泵102和粪便分解反应器112的污泥泵115定期抽吸污泥，通过污泥输送管116送入所述的固体物收集桶117，通过过滤网107进行固液分离，分离后的液体通过粪尿回流泵105再送入固液分离器108；
经所述的粪尿输送管118进入厌氧池200的粪尿，通过和所述的厌氧池生物膜201的反应，反应时间为20小时，粪尿经厌氧池200分解部分有机物，上清液通过厌氧自流管203进入所述的好氧池207，通过好氧池生物膜204和好氧曝气管206曝气，进一步降解粪尿有机物，反应时间20小时，粪尿污水进入所述的MBR反应器208，通过MBR自吸泵210及MBR反应器输送管209把经所述的好氧池生物膜204分离后的上清液送入所述的光催化氧化反应器300内，上清液通过紫外线灯301和臭氧曝气头302输出的臭氧进行有机物降解、消毒、杀菌、脱色；臭氧曝气头302的臭氧由氧气源臭氧发生器307通过臭氧管305供应；处理好的上清液通过所述的回用水输入管303进入回用水箱306，回用水通过回用水输出管304进入卫生间冲洗或绿化浇灌,所述的厌氧池排污泵202和所述的好氧池污泥输送泵(205)也定期抽吸污泥，通过污泥输送管116送入所述的固体物收集桶117。
实验表明，本实用新型不仅有效解决了粪尿污水直接排入下水管道，导致水资源的浪费和污染问题，而且有效解决了现有卫生间的废水回用问题及卫生间除臭的问题。
Claims (7)
1.一种卫生间粪尿资源化处理设备，其特征在于包括粪便分解系统、微生物处理系统和高级氧化系统：
所述的粪便分解系统包括固液分离器(108)、收集桶(106)、粪便分解反应器(112),所述的固液分离器(108)包含粪尿管(100)、分离板(101)、污泥泵、送粪管(103)、粪尿回流管(104)、自流液管(109)；所述的收集桶(106)包含粪尿回流泵(105)、过滤网(107)、固体物收集桶(117)；所述的粪便分解反应器(112)包含单向阀(110)、液位传感器(111)、粪尿输出泵(113)、分解微生物床(114)、污泥泵、污泥输送管(116)、粪尿输出管(118)；
所述的微生物处理系统包括厌氧池(200)、好氧池(207)、MBR反应器(208)；所述的厌氧池(200)包括厌氧池生物膜(201)、厌氧池排污泵(202)、厌氧自流管(203)；所述的好氧池(207)包含好氧池生物膜(204)、好氧池污泥输送泵(205)、好氧曝气管(206)、高压风机(211)；所述的MBR反应器(208)包括MBR反应器输送管(209)、MBR自吸泵(210)；
所述的高级氧化系统包括光催化氧化反应器(300)、回用水箱(306)；所述的光催化氧化反应器(300)包含紫外线灯(301)、臭氧曝气头(302)、臭氧管(305)、氧气源臭氧发生器(307)；所述的回用水箱(306)包含回用水输入管(303)、回用水输出管(304)；
所述的卫生间便器的粪尿经粪尿管(100)进入所述的固液分离器(108)，粪尿经所述的分离板(101)进行初步分离，固体粪便和卫生纸由送粪管(103)进入固体物收集桶(117)，通过过滤网(107)进行第二次过滤，过滤后的粪尿液体进入所述的收集桶(106)，由所述的粪尿回流泵(105)驱动经所述的粪尿回流管(104)回流到所述的固液分离器(108)进行再分离；分离后的液体粪尿通过自流液管(109)进入所述的粪便分解反应器(112)的下端，再通过分解微生物床(114)的分解、过滤后的液体上升到控制液位，触发液位传感器(111)，粪尿输出泵(113)驱动所述的粪尿经所述的粪尿输出管(118)进入厌氧池(200)，通过和所述的厌氧池生物膜(201)的反应分解部分有机物，上清液通过厌氧自流管(203)进入所述的好氧池(207)，通过好氧池生物膜(204)和好氧曝气管(206)曝气进一步降解粪尿有机物，粪尿污水进入所述的MBR反应器(208)，通过MBR自吸泵(210)及MBR反应器输送管(209)把经所述的好氧池生物膜(204)分离后的上清液送入所述的光催化氧化反应器(300)内，上清液通过紫外线灯(301)和臭氧曝气头(302)输出的臭氧进行有机物降解、消毒、杀菌和脱色处理；处理好的上清液通过所述的回用水输入管(303)进入回用水箱(306)，回用水通过回用水输出管(304)进入卫生间冲洗或绿化浇灌。
2.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述的粪尿输出管(118)安装有单向阀(110)，防止厌氧池(200)的粪尿液体回流。
3.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述的固液分离器(108)内的污泥泵和粪便分解反应器(112)的污泥泵定期抽吸污泥，通过污泥输送管(116)送入所述的固体物收集桶(117)，通过过滤网(107)进行固液分离，分离后的液体通过粪尿回流泵(105)再送入固液分离器(108)。
4.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述的粪尿和所述的厌氧池生物膜(201)的反应时间为20小时。
5.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述臭氧曝气头(302)的臭氧由氧气源臭氧发生器(307)通过臭氧管(305)供应。
6.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述的高压风机(211)供应好氧池(207)的曝气，提供微生物的溶解氧，进一步降解粪尿有机物。
7.根据权利要求1所述的卫生间粪尿资源化处理设备，其特征在于，所述的厌氧池排污泵(202)和所述的好氧池污泥输送泵(205)定期抽吸污泥，通过污泥输送管(116)送入所述的固体物收集桶(117)。
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| CN113072249A (zh) * | 2021-03-26 | 2021-07-06 | 广东四用科技有限公司 | 用复合材料负载微生物的粪尿处理系统及用其的移动厕所 |
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| CN111573888A (zh) * | 2020-05-20 | 2020-08-25 | 四川星辰心海生态环保科技有限公司 | 一种旅行列车卫生间废水处理装置及处理工艺 |
| CN113072249A (zh) * | 2021-03-26 | 2021-07-06 | 广东四用科技有限公司 | 用复合材料负载微生物的粪尿处理系统及用其的移动厕所 |
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