CN102603127B - 一种模块式生活垃圾和污水的源头处理装置及其处理方法 - Google Patents
一种模块式生活垃圾和污水的源头处理装置及其处理方法 Download PDFInfo
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- CN102603127B CN102603127B CN2012100974211A CN201210097421A CN102603127B CN 102603127 B CN102603127 B CN 102603127B CN 2012100974211 A CN2012100974211 A CN 2012100974211A CN 201210097421 A CN201210097421 A CN 201210097421A CN 102603127 B CN102603127 B CN 102603127B
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- 239000004571 lime Substances 0.000 claims description 5
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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[N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 claims description 3
- 238000005202 decontamination Methods 0.000 claims description 3
- 230000003588 decontaminative Effects 0.000 claims description 3
- 230000000249 desinfective Effects 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 3
- 229910001385 heavy metal Inorganic materials 0.000 claims description 3
- 150000002500 ions Chemical class 0.000 claims description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Abstract
本发明涉及一种模块式生活垃圾和污水的源头处理装置，包括粉碎机、挤压式固液分离机、生活污水排放总管、生物厌氧反应器、沸石分子筛装置、储水箱，与沸石分子筛装置连接臭氧曝气器和反冲洗水泵，储水箱的底部设有曝气管，并通过以下处理方法即粉碎、提取、搅拌、固液分离、厌氧反应、脱污处理、污水净化、循环净化、净化利用、固体垃圾收集等步骤，使得源头减量效果明显，可应用于污水的就地处理，效率极高、分解彻底，源头减量效果明显，有利于推进垃圾分类收集，降低了垃圾运输过程中环境污染，减少了污水市政管网，大大减少了投资费用，从根本上解决了集中处置的种种不足，真正从源头进行处理。另外本发明投资小、见效快、零污染，小型方便，使用灵活等优点。
Description
一种模块式生活垃圾和污水的源头处理装置及其处理方法
技术领域
[0001] 本发明属于生活垃圾处理技术领域，特别是涉及一种模块式生活垃圾和污水的源头处理装置及其处理方法。
背景技术
[0002] 城市垃圾处理问题已经成为当今世界环保领域中的一项重大研究课题。随着世界各地城市的迅猛发展，城市垃圾的数量在全球范围内迅速增长，垃圾中的有害成分对大气、水体、土壤等造成严重危害，影响城市生态环境，危害人民群众身体健康，已成为世界公害。我国大部分城市也已处于垃圾包围之中，垃圾处理成了世界关注的难题。
[0003] 随着城市燃气化程度加快，城市垃圾中的煤渣、煤灰已不多见，有机垃圾的比重越来越高。垃圾源头分类处理就是一种新型的处理方法，所谓的源头处理是在进入市政管网前进行就进行合理的处理。要想让垃圾变成资源，必须进行源头有效分类和处理，如果不能进行源头分类的垃圾，那么永远是垃圾。
[0004] 当前有机垃圾处理大多是建设大型的垃圾处理厂，处理方法大致有3种:填埋法、焚烧法、堆肥法都是先进行垃圾集中收集，运送至一级垃圾处理中心进行初处理，再运至更高级的处置中心进行深度处理。此处理过程中，垃圾运输过程中的污水有滴漏现象，造成城市环境的二次污染、滋生蚊蝇、发出恶臭等。
[0005] 当前我国处理污废水的方法主要是通过市政管网集中收集处理，耗资量大，而且建大型污水处理厂投资巨大，处理量却有限，周期较长，设备的故障多、寿命短、维修量大。
[0006] 因此，城市居民生活垃圾和污水的处理方法亟待改善，模块式生活垃圾及污水源头清洁利用处理装置及方法应运而生。 发明内容
[0007] 本发明为解决公知技术中存在的技术问题而提供一种零污染、无排放，且能供应小区内厕所与绿化用水的模块式生活垃圾和污水的源头处理装置及其处理方法。。
[0008] 本发明为解决公知技术中存在的技术问题所采取的技术方案是:
[0009] 一种模块式生活垃圾和污水的源头处理装置，包括粉碎机、挤压式固液分离机、生活污水排放总管、生物厌氧反应器、沸石分子筛装置、储水箱，其特征在于:所述粉碎机的出口处设有的接料箱，所述接料箱内设有提升泵，所述提升泵通过输送管连接集污池，所述集污池内设有搅拌器和潜水泵，所述潜水泵通过输送管道连接挤压式固液分离机，所述挤压式固液分离机的底部设有出液管，所述出液管连接生物厌氧反应器进料总管，所述进料总管还连接生活污水排放总管，所述生物厌氧反应器内设有厌氧菌富集膜；所述生物厌氧反应器的出料管连接沸石分子筛装置，所述沸石分子筛装置连接臭氧曝气器和反冲洗水泵，所述臭氧曝气器的出气管连接曝气管和反冲洗进气管，所述曝气管位于沸石分子筛的底部，反冲洗进气管位于沸石分子筛顶部；所述反冲洗水泵的出水管连接反冲洗水管，所述反冲洗水管位于沸石分子筛顶部；所述沸石分子筛装置的顶部设有出水管，所述出水管连接出水泵的进水口，沸石分子筛装置的底部设有反冲洗出水管，所述出水泵的出水口通过出水管连接储水箱的进水口，所述储水箱的底部设有曝气管，所述曝气管通过输气管连接臭氧曝气器，所述储水箱的出水口通过输水管连接市政管网。
[0010] 本发明还可以采用如下技术措施:
[0011] 该处理装置还包括太阳能发电装置。
[0012] 该处理装置还包括自动化控制系统。
[0013] 利用上述模块式生活垃圾和污水的源头处理装置处理生活垃圾和污水的方法，其特征在于:该处理方法包括如下步骤:
[0014] I)、粉碎:将由可降解的环保袋收集的初始复合垃圾，在粉碎机内粉碎，粉碎后的混合物料放直在接料箱内；
[0015] 2)、提取:通过提升泵将接料箱内的混合物料提取到集污池内；
[0016] 3)、搅拌:在集污池内开启搅拌器，将集污池内的混合物料搅拌均匀；
[0017] 4)、固液分离:在上述搅拌的同时开启集污池内的潜水泵，通过潜水泵将搅拌均匀的混合物料输送挤压式 固液分离机内，并通过密封过程将块状固体运输到固体处理中心，分离出的液体由管道输入送到生物厌氧反应器；
[0018] 5)、厌氧反应:在生物厌氧反应器内进行周期性反应，反应周期为4小时，反应周期结束后自动进入沸石分子筛装置内；
[0019] 6)、脱污处理:通过沸石分子筛装置内的沸石分子筛脱除污水中的氨氮、磷、有机物、放射性污染物，并吸附重金属离子，达到净化污水的的目的；
[0020] 7)、污水净化:通过开启与分子筛装置连通的臭氧曝气器，实现臭氧与空气进行间歇式曝气，进一步净化污水；
[0021] 8)、循环净化:在上述净化过程中间歇开启反冲洗水泵和反冲洗气管，通过反冲洗水管和反冲洗气管冲洗沸石分子筛，实现循环净化，经过上述净化的水通过出水泵提取到储水箱内；
[0022] 9)、净化利用:开启与储水箱连接的臭氧曝气器，通过臭氧曝气器再次进行消毒净化，净化后的水直接与市政管网的马桶冲水或者绿化用水系统连接；
[0023] 10)、固体垃圾收集:将上述步骤分离出的固体不可回收利用垃圾通过垃圾压块机集中进行压块，并将垃圾压块集中收集在块状垃圾储存罐内，并定期运往块状垃圾处理中心进行处理。
[0024] 本发明具有的优点和积极效果是:由于本发明采用上述技术方案，使得本发明具有以下优点:
[0025] 1、源头减量效果明显。可应用于污水的就地处理，效率极高、分解彻底，源头减量效果明显。
[0026] 2、有利于推进垃圾分类收集。可在源头实现分类垃圾后续分类处理的部分配套，垃圾仅按有机垃圾和无机垃圾分类收捡。有机垃圾在专门的处置中心可作为再生资源回收利用或综合处理，有利于推进垃圾分类收集，快速提升垃圾分类收集率。
[0027] 3、降低了垃圾运输过程中环境污染。同时，垃圾经挤压式固液分离后，垃圾的含水率明显下降，减少了垃圾运输过程中的污水滴漏现象，也能改善垃圾运输过程中的恶臭现象。[0028] 4、减少了污水市政管网建设，大大减少了投资费用，从根本上解决了集中处置的种种不足，真正从源头进行处理。
[0029] 另外，本发明投资小、见效快、零污染，小型方便，使用灵活等优点。真正做到了垃圾与污水处理的源头减量化、无害化、资源化、循环化。
附图说明
[0030] 图1是本发明的结构示意图。
[0031] 图中:1、粉碎机；2、挤压式固液分离机；3、生活污水排放总管；4、生物厌氧反应器；4_1、厌氧菌富集膜；5、沸石分子筛装置；5-1、沸石分子筛；6、储水箱；7、接料箱；8、提升泵；9、集污池；10、搅拌器；11、潜水泵；12、输送管；13、出液管；14、臭氧曝气器；15、反冲洗水泵；16、曝气管；17、反冲洗进气管；18、反冲洗水管；19、出水管；20、出水泵；21、反冲洗出水管；22、曝气管；23、臭氧曝气器；24、太阳能发电装置；25、自动化控制系统；26、垃圾压块机；27、储存罐；28、输水管。
具体实施方式
[0032] 为能进一步了解本发明的发明内容、特点及功效，兹例举以下实施例，并配合附图详细说明如下:
[0033] 请参阅图1，一种模块式生活垃圾和污水的源头处理装置，包括粉碎机1、挤压式固液分离机2、生活污水排放总管3、生物厌氧反应器4、沸石分子筛装置5、储水箱6，上述设备中粉碎机1、挤压式固液分离机2、生物厌氧反应器4、沸石分子筛装置均属于现有技术，其工作原理和结构在此不做描述， 在市场上均可以购买或者购买散件进行组装，而且沸石分子筛中的沸石，是一种天然、无毒、无味且对环境没有影响的吸附剂，且该装置方便拆卸、冲洗。所述粉碎机I的出口处设有的接料箱7，所述接料箱7内设有提升泵8，所述提升泵8通过输送管连接集污池9，所述集污池9内设有搅拌器10和潜水泵11，所述潜水泵11通过输送管12接挤压式固液分尚机2,所述挤压式固液分尚机2的底部设有出液管13,所述出液管13连接生物厌氧反应器4进料总管，所述进料总管还连接生活污水排放总管3，所述生物厌氧反应器4内设有厌氧菌富集膜4-1 ;所述生物厌氧反应器4的出料管连接沸石分子筛装置5，所述沸石分子筛装置5连接臭氧曝气器14和反冲洗水泵15，所述臭氧曝气器14的出气管连接曝气管16和反冲洗进气管17，所述曝气管16位于沸石分子筛5-1的底部，反冲洗进气管17位于沸石分子筛5-1顶部；所述反冲洗水泵15的出水管连接反冲洗水管18，所述反冲洗水管18位于沸石分子筛5-1顶部；所述沸石分子筛装置5的顶部设有出水管19，所述出水管19连接出水泵20的进水口，沸石分子筛装置的底部设有反冲洗出水管21，所述出水泵20的出水口通过出水管连接储水箱6的进水口，所述储水箱21的底部设有曝气管22，所述曝气管22通过输气管连接臭氧曝气器23，所述储水箱21的出水口通过输水管28连接市政管网。
[0034] 本发明还可以采用如下技术措施:
[0035] 该处理装置还包括太阳能发电装置24。所述上述装置中所需用电部分由太阳能板与市政电网共同提供，太阳能供应不足时由市政电网提供。其主要目的，节约部分电能。
[0036] 为便于实现自动远程控制，该处理装置还包括自动化控制系统25，该控制系统可以根据实际需购买相关器件进行设计，主要是控制粉碎机1、挤压式固液分离机2、提升泵8、搅拌器10和潜水泵11、臭氧曝气器等需要开启和关闭控制的设备，并且设计开启时间和频率等。该控制系统的设计对于本领域技术人员是较为常见的设计，因此具体设计控制方式在此不做过多描述，
[0037] 利用上述模块式生活垃圾和污水的源头处理装置处理生活垃圾和污水的方法，该处理方法包括如下步骤:
[0038] 1)、粉碎:将由可降解的环保袋收集的初始复合垃圾，在粉碎机内粉碎，粉碎后的混合物料放直在接料箱内；
[0039] 2)、提取:通过提升泵将接料箱内的混合物料提取到集污池内；
[0040] 3)、搅拌:在集污池内开启搅拌器，将集污池内的混合物料搅拌均匀；
[0041] 4)、固液分离:在上述搅拌的同时开启集污池内的潜水泵11，通过潜水泵将搅拌均匀的混合物料输送挤压式固液分离机2内，并通过密封过程将块状固体运输到固体处理中心，分离出的液体由管道输入送到生物厌氧反应器4;步骤中的密封输送过程，即在密封状态下输送块状垃圾，以防止臭味外泄的目的，例如在密封管道内或者密封容器内进行输送，该种输送方式较为常见，具体采用什么输送方式再次不做详细表述。
[0042] 5)、厌氧反应:在生物厌氧反应器4内进行周期性反应，反应周期为4小时，反应周期结束后自动进入沸石分子筛装置5内；
[0043] 6)、脱污处理:通过沸石分子筛装置5内的沸石分子筛脱除污水中的氨氮、磷、有机物、放射性污染物，并吸附重金属离子，达到净化污水的的目的；
[0044] 7)、污水净化:通过开启与沸石分子筛装置5连通的臭氧曝气器14，实现臭氧与空气进行间歇式曝气，进一步净化污水；
[0045] 8)、循环净化:在上述净化过程中间歇开启反冲洗水泵15和反冲洗气管17，通过反冲洗水管18和反冲洗气管17冲洗沸石分子筛，防止堵塞，并实现循环净化，经过上述净化的水通过出水泵20提取到储水箱21内；
[0046] 9)、净化利用:开启与储水箱21连接的臭氧曝气器23，通过臭氧曝气器再次进行消毒净化，净化后的水直接与市政管网的马桶冲水或者绿化用水系统连接；
[0047] 10)、固体垃圾收集:将上述步骤分离出的固体不可回收利用垃圾通过垃圾压块机26集中进行压块，并将垃圾压块集中收集在块状垃圾储存罐27内，并定期运往块状垃圾处理中心进行处理。
[0048] 综上所述本发明具有以下优点:
[0049] 1、源头减量效果明显。可应用于污水的就地处理，效率极高、分解彻底，源头减量效果明显。
[0050] 2、有利于推进垃圾分类收集。可在源头实现分类垃圾后续分类处理的部分配套，垃圾仅按有机垃圾和无机垃圾分类收捡。有机垃圾在专门的处置中心可作为再生资源回收利用或综合处理，有利于推进垃圾分类收集，快速提升垃圾分类收集率。
[0051] 3、降低了垃圾运输过程中环境污染。同时，垃圾经挤压式固液分离后，垃圾的含水率明显下降，减少了垃圾运输过程中的污水滴漏现象，也能改善垃圾运输过程中的恶臭现象。
[0052] 4、减少了污水市政管网建设，大大减少了投资费用，从根本上解决了集中处置的种种不足，真正从源头进行处理。
[0053] 另外，本发明投资小、见效快、零污染，小型方便，使用灵活等优点。真正做到了垃圾与污水处理的源头减量 化、无害化、资源化、循环化。
Claims (4)
1.一种模块式生活垃圾和污水的源头处理装置，包括粉碎机、挤压式固液分离机、生活污水排放总管、生物厌氧反应器、沸石分子筛装置、储水箱，其特征在于:所述粉碎机的出口处设有的接料箱，所述接料箱内设有提升泵，所述提升泵通过输送管连接集污池，所述集污池内设有搅拌器和潜水泵，所述潜水泵通过输送管道连接挤压式固液分离机，所述挤压式固液分离机的底部设有出液管，所述出液管连接生物厌氧反应器进料总管，所述进料总管还连接生活污水排放总管，所述生物厌氧反应器内设有厌氧菌富集膜；所述生物厌氧反应器的出料管连接沸石分子筛装置，所述沸石分子筛装置连接臭氧曝气器和反冲洗水泵，所述臭氧曝气器的出气管连接曝气管和反冲洗进气管，所述曝气管位于沸石分子筛的底部，反冲洗进气管位于沸石分子筛顶部；所述反冲洗水泵的出水管连接反冲洗水管，所述反冲洗水管位于沸石分子筛顶部；所述沸石分子筛装置的顶部设有出水管，所述出水管连接出水泵的进水口，沸石分子筛装置的底部设有反冲洗出水管，所述出水泵的出水口通过出水管连接储水箱的进水口，所述储水箱的底部设有曝气管，所述曝气管通过输气管连接臭氧曝气器，所述储水箱的出水口通过输水管连接市政管网。
2.根据权利要求1所述的模块式生活垃圾和污水的源头处理装置，其特征在于:该处理装置还包括太阳能发电装置。
3.根据权利要求1或2所述的模块式生活垃圾和污水的源头处理装置，其特征在于:该处理装置还包括自动化控制系统。
4.利用上述任一权利要求所述的模块式生活垃圾和污水的源头处理装置处理生活垃圾和污水的方法，其特征在于:该处理方法包括如下步骤: 1)、粉碎:将由可降解的环保袋收集的初始复合垃圾，在粉碎机内粉碎，粉碎后的混合物料放置在接料箱内； 2)、提取:通过提升泵将接料箱内的混合物料提取到集污池内； 3)、搅拌:在集污池内开启搅拌器，将集污池内的混合物料搅拌均匀； 4)、固液分离:在上述搅拌的同时开启集污池内的潜水泵，通过潜水泵将搅拌均匀的混合物料输送挤压式固液分离机内，并通过密封过程将块状固体运输到固体处理中心，分离出的液体由管道输入送到生物厌氧反应器； 5)、厌氧反应:在生物厌氧反应器内进行周期性反应，反应周期为4小时，反应周期结束后自动进入沸石分子筛装置内； 6)、脱污处理:通过沸石分子筛装置内的沸石分子筛脱除污水中的氨氮、磷、有机物、放射性污染物，并吸附重金属离子，达到净化污水的的目的； 7)、污水净化:通过开启与分子筛装置连通的臭氧曝气器，实现臭氧与空气进行间歇式曝气，进一步净化污水； 8)、循环净化:在上述净化过程中间歇开启反冲洗水泵和反冲洗气管，通过反冲洗水管和反冲洗气管冲洗沸石分子筛，实现循环净化，经过上述净化的水通过出水泵提取到储水箱内； 9)、净化利用:开启与储水箱连接的臭氧曝气器，通过臭氧曝气器再次进行消毒净化，净化后的水直接与市政管网的马桶冲水或者绿化用水系统连接； 10)、固体垃圾收集:将上述步骤分离出的固体不可回收利用垃圾通过垃圾压块机集中进行压块，并将垃圾压块集中收集在块状垃圾储存罐内，并定期运往块状垃圾处理中心进行 处理。
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