CN101311131A - Sewage handling method and uses thereof - Google Patents
Sewage handling method and uses thereof Download PDFInfo
- Publication number
- CN101311131A CN101311131A CNA2007100113974A CN200710011397A CN101311131A CN 101311131 A CN101311131 A CN 101311131A CN A2007100113974 A CNA2007100113974 A CN A2007100113974A CN 200710011397 A CN200710011397 A CN 200710011397A CN 101311131 A CN101311131 A CN 101311131A
- Authority
- CN
- China
- Prior art keywords
- water
- sewage
- domestic sewage
- filter
- ozone oxidation
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 61
- 238000000034 method Methods 0.000 title claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 82
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 31
- 239000001301 oxygen Substances 0.000 claims abstract description 31
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 24
- 230000003647 oxidation Effects 0.000 claims abstract description 17
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 17
- 238000011010 flushing procedure Methods 0.000 claims abstract description 12
- 238000003860 storage Methods 0.000 claims abstract description 9
- 239000007787 solid Substances 0.000 claims abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 17
- 230000015556 catabolic process Effects 0.000 claims description 8
- 238000006731 degradation reaction Methods 0.000 claims description 8
- 230000001580 bacterial effect Effects 0.000 claims description 6
- 229910052902 vermiculite Inorganic materials 0.000 claims description 5
- 235000019354 vermiculite Nutrition 0.000 claims description 5
- 239000010455 vermiculite Substances 0.000 claims description 5
- 238000011081 inoculation Methods 0.000 claims description 2
- 239000002054 inoculum Substances 0.000 claims description 2
- 239000000706 filtrate Substances 0.000 claims 5
- 238000003672 processing method Methods 0.000 claims 5
- 230000000813 microbial effect Effects 0.000 claims 3
- 230000001954 sterilising effect Effects 0.000 claims 3
- 241000193830 Bacillus <bacterium> Species 0.000 claims 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 2
- 241000588986 Alcaligenes Species 0.000 claims 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims 1
- 238000011001 backwashing Methods 0.000 claims 1
- 238000011109 contamination Methods 0.000 claims 1
- 229910001882 dioxygen Inorganic materials 0.000 claims 1
- 239000003292 glue Substances 0.000 claims 1
- 230000005484 gravity Effects 0.000 claims 1
- 238000002203 pretreatment Methods 0.000 claims 1
- 238000005273 aeration Methods 0.000 abstract description 22
- 238000005516 engineering process Methods 0.000 abstract description 6
- 239000002245 particle Substances 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000011112 process operation Methods 0.000 abstract 1
- 239000000463 material Substances 0.000 description 15
- 230000000593 degrading effect Effects 0.000 description 10
- 241000894006 Bacteria Species 0.000 description 9
- 239000003344 environmental pollutant Substances 0.000 description 5
- 231100000719 pollutant Toxicity 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 239000000571 coke Substances 0.000 description 4
- 238000010411 cooking Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000013461 design Methods 0.000 description 3
- 239000002957 persistent organic pollutant Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 241000588810 Alcaligenes sp. Species 0.000 description 2
- 241000194110 Bacillus sp. (in: Bacteria) Species 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 2
- 239000010775 animal oil Substances 0.000 description 2
- 238000003287 bathing Methods 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 239000006004 Quartz sand Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 241000227149 Zoogloea sp. Species 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000032770 biofilm formation Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002550 fecal effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 235000019198 oils Nutrition 0.000 description 1
- 238000006385 ozonation reaction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
Images
Classifications
-
- 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
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
本发明涉及城市社区污水处理与中水回用技术,具体地说是一种生活污水处理方法及其应用。具体为生活污水经格栅进入集水池,将已去除较大固体颗粒的生活污水通过抽水泵并经过滤器使生活污水抽到预处理后的微氧曝气滤池中降解污水中的有机污染,降解后的水经微氧曝气滤池的出水口自流到臭氧氧化消毒器进行臭氧氧化,氧化后的水经臭氧氧化消毒器出水口自流存放到贮存池;处理后的再生水作为冲洗便池用水,冲厕后直接排入市政污水管网。本发明大幅度降低了处理成本,其工艺操作简单、实用、操作方便,处理效率高、再生水水质优良、回用率高,通过本发明工艺可减少社区污水排放量50%,实现中水回收利用减少水消耗量30-40%。The invention relates to urban community sewage treatment and middle water reuse technology, in particular to a domestic sewage treatment method and its application. Specifically, the domestic sewage enters the sump through the grid, and the domestic sewage from which large solid particles have been removed is pumped through the pump and filtered to the pretreated micro-aerobic aeration filter to degrade the organic pollution in the sewage. The degraded water flows through the outlet of the micro-oxygen aeration filter to the ozone oxidation sterilizer for ozone oxidation, and the oxidized water flows through the outlet of the ozone oxidation sterilizer to the storage pool; the treated regenerated water is used as water for flushing the urinal , directly discharged into the municipal sewage pipe network after flushing the toilet. The invention greatly reduces the treatment cost, and its process operation is simple, practical, convenient to operate, high in treatment efficiency, excellent in regenerated water quality, and high in reuse rate. The process of the invention can reduce community sewage discharge by 50%, and realize the recycling of reclaimed water Reduce water consumption by 30-40%.
Description
技术领域 technical field
本发明涉及城市社区污水处理与中水回用技术,具体地说是一种生活污水处理方法及其应用。The invention relates to urban community sewage treatment and reclaimed water technology, in particular to a domestic sewage treatment method and its application.
背景技术 Background technique
目前,我国城市居民人均生活用水量约为150L/d,其中冲洗厕所用水量占有很大比例,一般单次冲水量为6-8L,按照每日8次计,每日厕所用水约为居民日用水量的40%。应用再生水取代纯净水冲厕,城市生活用水量即可减少40%。At present, the per capita domestic water consumption of urban residents in my country is about 150L/d, of which the water consumption for flushing toilets accounts for a large proportion. Generally, the single flushing volume is 6-8L. Based on 8 times a day, the daily toilet water consumption is about 150L/d. 40% of water usage. Using recycled water instead of pure water for toilet flushing can reduce urban water consumption by 40%.
上世纪90年代,集社区生活污水处理与回用于一体的地下渗滤系统曾在中水回用方面发挥了重要作用,但该技术只适用于社区居民密度较小、建筑物间绿地面积较大的条件。随着城市高层住宅的普及,单位面积居民负荷率成倍提高,人均绿地面积大幅度下降,采用占地面积较大的地下渗滤处理工艺已比较困难。In the 1990s, the underground infiltration system integrating community domestic sewage treatment and reuse played an important role in the reuse of reclaimed water, but this technology is only suitable for communities with low density of residents and large green areas between buildings. big condition. With the popularization of high-rise residential buildings in cities, the load rate of residents per unit area has doubled, and the per capita green area has dropped significantly. It has become more difficult to adopt underground infiltration treatment processes that occupy a large area.
现有的社区污水处理与中水回用工艺,一般均采用污水全部收集、处理、回用的方法,当中水用于冲洗厕所后即进入下一个循环,使得污水可生化性随时间推移而变坏,增加了处理难度与成本。同时随着居民生活水平提高,人均水消耗量逐步增加,污水COD浓度呈下降趋势,对经济技术指标造成不利影响。The existing community sewage treatment and reclaimed water reuse process generally adopts the method of collecting, treating and reusing all the sewage. The reclaimed water enters the next cycle after being used to flush the toilet, so that the biodegradability of the sewage changes with time. Bad, increased processing difficulty and cost. At the same time, with the improvement of residents' living standards, the per capita water consumption gradually increases, and the COD concentration of sewage shows a downward trend, which has a negative impact on economic and technical indicators.
基于上述考虑,从根本上改变现有社区污水就地处理与就地回用工艺,研究建立在新理念基础上的小区污水处理与回用技术,将具有良好的应用前景与巨大的社会经济与环境效益。Based on the above considerations, fundamentally changing the existing community sewage treatment and reuse process on site, and researching community sewage treatment and reuse technology based on new concepts will have good application prospects and huge social, economic and social benefits. environmental benefits.
一般家庭生活用水可分为厨房烹饪用水、日常盥洗用水、洗衣用水与洗浴用水以及冲厕用水四种类型。其中冲厕用水量占总用水量的40%,但其污染负荷则占总污染负荷的80%。如将前三种污水单独收集处理,则不但其处理难度大大降低,处理后产生的中水可基本上满足冲厕需要。Generally, household water can be divided into four types: kitchen cooking water, daily toilet water, laundry water, bath water, and toilet flushing water. Among them, the water consumption for toilet flushing accounts for 40% of the total water consumption, but its pollution load accounts for 80% of the total pollution load. If the first three kinds of sewage are collected and treated separately, not only the difficulty of treatment will be greatly reduced, but the reclaimed water produced after treatment can basically meet the needs of toilet flushing.
根据我国城市小区建筑发展趋势与小区水处理与回用的实际情况,在长期研究基础上,提出了小区污水处理与回用结合的新型技术。According to the development trend of urban community buildings in my country and the actual situation of water treatment and reuse in the community, on the basis of long-term research, a new technology for the combination of sewage treatment and reuse in the community is proposed.
发明内容 Contents of the invention
本发明的目的是提供一种经济、实用、高效、环保并且适用广泛的生活污水处理工艺及其应用。The object of the present invention is to provide an economical, practical, efficient, environmentally friendly and widely applicable domestic sewage treatment process and its application.
为了实现上述目的,本发明的技术方案是:In order to achieve the above object, technical scheme of the present invention is:
处理方法:生活污水经格栅1进入集水池2,将已去除较大固体颗粒的生活污水通过抽水泵3并经过滤器4使生活污水抽到预处理后的微氧曝气滤池5中降解污水中的有机污染,降解后的水经微氧曝气滤池5的出水口自流到臭氧氧化消毒器7进行臭氧氧化,氧化后的水经臭氧氧化消毒器7出水口自流存放到贮存池10;Treatment method: the domestic sewage enters the
其中,微氧曝气滤池5的预处理:微氧曝气滤池5内投放占该池容积2/3的滤料,同时接种降解菌种,接种量按照待处理生活污水体积的百分比计为2%-5%,并通入氧气,氧气流速0.010m3/min-0.012m3/min,使其形成一层生物膜。Among them, the pretreatment of the micro-aerobic aeration filter 5: the filter material accounting for 2/3 of the volume of the pool is put into the
所述降解菌种为芽孢杆菌(Bacillus sp.)、产碱杆菌(Alcaligenes sp.)和动胶杆菌(Zoogloea sp.),其体积份数比为1∶1∶1;其中:所述滤料为活性焦碳和蛭石,其按重量比为1∶1。The degrading bacteria species are Bacillus sp., Alcaligenes sp. and Zoogloea sp., and the volume-to-number ratio is 1:1:1; wherein: the filter material It is activated coke and vermiculite in a weight ratio of 1:1.
微氧曝气滤池5形成生物膜时,滤料和降解菌种在生活污水内,室温下进行培养,每隔4-6天换一次培养滤料和降解菌种的用水,每次换水量占培养滤料和降解菌种所用水总水量的50%-60%,培养25-40天,即形成一层生物膜。When the
水力停留时间4-6h。反冲洗周期20天;臭氧氧化消毒器7内的臭氧浓度为40-100mg/L。The hydraulic retention time is 4-6h. The backwash cycle is 20 days; the ozone concentration in the
处理方法的应用:城市居民小区、宾馆、学校;同时处理后的污水用于冲洗便池。Application of treatment methods: urban residential quarters, hotels, schools; at the same time, the treated sewage is used for flushing urinals.
本发明的原理:采用微氧曝气滤池是将空压机产生的氧用强制的方法溶解到混合污水中,曝气除起供氧外,还起搅拌作用,保证与吸附在滤料表面上的微生物充分接触,并快速降解。上流式生物滤池,氧气与污水均从滤池底部进入,其目的是有利于污水中的污染物与微生物充分接触,保证处理效果。同时生活污水中较难降解的有机污染物来源于洗涤水的表面活性剂和烹饪水的油脂。本发明的微氧曝气滤池内接种经培养、驯化的洗涤剂和动植物油高效降解菌剂,待滤料表面形成一层生物膜。生物膜具有对有机污染物的降解活性,生物膜形成的成功与否关系到污染物的去除效果。并且为保证经微氧曝气滤池处理后的再生水符合中水标准,采用臭氧消毒对其进行深度处理,以进一步降低COD负荷并杀死水中病原菌。臭氧浓度控制在40-100mg/L范围,可保证出水中总大肠菌数小于3个L-1,符合中水指标要求。The principle of the present invention: the use of micro-oxygen aeration filter is to dissolve the oxygen produced by the air compressor into the mixed sewage in a forced way. In addition to supplying oxygen, the aeration also plays a stirring role to ensure and adsorb on the surface of the filter material. Fully contact with microorganisms on the surface, and quickly degrade. In the upflow biological filter, both oxygen and sewage enter from the bottom of the filter, the purpose of which is to facilitate the full contact between the pollutants in the sewage and the microorganisms, and ensure the treatment effect. At the same time, the organic pollutants that are difficult to degrade in domestic sewage come from the surfactant in washing water and the oil in cooking water. The micro-oxygen aeration filter of the present invention is inoculated with cultured and domesticated detergent and animal and vegetable oil high-efficiency degradation bacterial agents, and a layer of biofilm is formed on the surface of the filter material. Biofilm has the ability to degrade organic pollutants, and the success of biofilm formation is related to the removal effect of pollutants. And in order to ensure that the regenerated water treated by the micro-oxygen aeration filter meets the standard of reclaimed water, ozone disinfection is used for advanced treatment to further reduce the COD load and kill pathogenic bacteria in the water. The ozone concentration is controlled in the range of 40-100mg/L, which can ensure that the total number of coliform bacteria in the effluent water is less than 3 L -1 , in line with the requirements of reclaimed water indicators.
与现有技术相比,本发明具有如下优点:Compared with prior art, the present invention has following advantage:
1.本发明工艺简单可行、实用、操作方便,处理效率高、再生水水质优良、回用率高的优点,本发明半开放式循环可有效避免污水可生化性变差的问题,实现系统长期稳定运行,通过本发明工艺可减少社区污水排放量50%,实现中水回收利用减少水消耗量30-40%。1. The process of the present invention is simple, feasible, practical, easy to operate, high in treatment efficiency, excellent in regenerated water quality, and high in reuse rate. The semi-open cycle of the present invention can effectively avoid the problem of poor biodegradability of sewage and achieve long-term stability of the system In operation, the process of the invention can reduce community sewage discharge by 50%, realize reclaimed water recycling and reduce water consumption by 30-40%.
2.本发明微氧曝气滤池中具有对有机污染物有降解活性的膜,可保证生活污水中的污染物洗涤剂类和油脂类污染物去除效果。2. The micro-aerobic aeration filter of the present invention has a membrane with degradation activity for organic pollutants, which can ensure the removal effect of pollutant detergents and grease pollutants in domestic sewage.
3.对污染物处理比较彻底,本发明利用上流式微氧过滤系统、过滤器、臭氧氧化消毒器技术等多级处理,处理效率高,使再生水水质优良。3. The treatment of pollutants is relatively thorough. The present invention utilizes multi-stage treatment such as an upflow micro-oxygen filtration system, filter, and ozone oxidation sterilizer technology, so that the treatment efficiency is high and the regenerated water quality is excellent.
3.本发明可根据城市居民小区、宾馆学校等具体情况设计不同规模,例如300人当量,可设计集水池、微氧曝气滤池和贮存池容积15m3,其结构简单、成本低廉、适应性广。3. The present invention can design different scales according to the specific conditions of urban residential areas, hotels and schools, etc., such as 300 equivalents, and can design a water collection tank, a micro-oxygen aeration filter tank and a storage tank with a volume of 15m 3 , which is simple in structure, low in cost, and adaptable. wide range.
4.采用本发明将城市生活污水,例如收集的厨房烹饪用水、日常盥洗用水、洗衣用水与洗澡用水处理后再利用,一方面减少了新鲜自来水用量,同时也减少了污水排放量。对于城市居民小区、宾馆、学校、饭店等具有良好的经济效益和广泛的应用前景。4. Using the present invention to reuse urban domestic sewage, such as collected kitchen cooking water, daily washing water, laundry water and bathing water, on the one hand reduces the consumption of fresh tap water, and also reduces the amount of sewage discharge. It has good economic benefits and broad application prospects for urban residential quarters, hotels, schools, restaurants, etc.
附图说明 Description of drawings
图1为本发明城市社区生活污水处理与回用工艺流程图。Fig. 1 is the flow chart of the present invention for urban community domestic sewage treatment and reuse process.
图2为本发明生活污水处理工艺流程图。Fig. 2 is a flow chart of the domestic sewage treatment process of the present invention.
1.格栅,2.集水池,3.抽水泵,4.过滤器,5.微氧曝气滤池,6.空压机,7.臭氧氧化消毒器,8.臭氧发生器,9.氧气瓶,10.贮存池1. Grille, 2. Pool, 3. Suction pump, 4. Filter, 5. Micro-oxygen aeration filter, 6. Air compressor, 7. Ozone oxidation sterilizer, 8. Ozone generator, 9. Oxygen cylinders, 10. Storage pools
具体实施方式 Detailed ways
下面结合实施例对本发明做进一步详细说明。The present invention will be described in further detail below in conjunction with the examples.
实施例1Example 1
微氧曝气滤池5的预处理:在微氧曝气滤池5内投放占其容积2/3的滤料活性焦碳和蛭石,而后投加生活污水使滤料和降解菌种在其环境,并在室温条件下生长,其接种降解菌种时,按体积百分比计,降解菌种接种量为:滤料和降解菌种生长时投加的生活污水体积的2.5%,并间歇式通氧气,氧气流速0.012m3/min,在室温20℃-28℃条件下运行,每隔5天换一次培养滤料和降解菌种所用的水,换水量占培养滤料和降解菌种所用水总水量的50%,经过35天运行即形成一层生物膜:其中:活性焦碳和蛭石之间的重量比为1∶1,并且微氧曝气滤池5内水位高于滤料;所述降解菌种为芽孢杆菌(Bacillus sp.)、产碱杆菌(Alcaligenes sp.)和动胶杆菌(Zoogloeasp.),其体积份数比为1∶1∶1;其中:所述滤料为活性焦碳和蛭石,其按重量比为1∶1。Pretreatment of the micro-oxygen aeration filter 5: put filter material activated coke and vermiculite accounting for 2/3 of its volume in the micro-oxygen aeration filter 5, and then add domestic sewage to make the filter material and degradation bacteria in the micro-oxygen aeration filter 5 Its environment, and grows under the room temperature condition, when it inoculates the degrading strain, by volume percentage, the inoculum amount of the degrading strain is: 2.5% of the domestic sewage volume added when the filter material and the degrading strain grow, and intermittently Oxygen flow, oxygen flow rate 0.012m 3 /min, operating at a room temperature of 20°C-28°C, changing the water used for cultivating filter materials and degrading bacteria every 5 days, the amount of water exchanged accounted for the cultivation of filter materials and degrading bacteria 50% of the total amount of water is used, and a layer of biofilm is formed after 35 days of operation: wherein: the weight ratio between activated coke and vermiculite is 1: 1, and the water level in the micro-aerobic aeration filter tank 5 is higher than the filter material ; The degrading strains are Bacillus sp., Alcaligenes sp. and Zoogloeasp., and the volume-to-number ratio is 1:1:1; wherein: the filter material It is activated coke and vermiculite in a weight ratio of 1:1.
分别取厨房烹饪污水、盥洗污水、洗衣污水与洗浴污水各2L,共8L,经过间隙为2mm的不锈钢材质的格栅1,去除较大固体颗粒后污水进入集水池2,此时集水池2中污水水质综合指标CODcr为52mg/L,BOD5为29mg/L,pH为7.6,SS为18mg/L(参见表1)进入集水池2的污水通过抽水泵3再经过滤器4使生活污水抽到微氧曝气滤池5中降解污水中的有机污染,并通过空压机6向微氧曝气滤池5内充氧,降解后的水经微氧曝气滤池5的出水口自流到臭氧氧化消毒器7进行臭氧氧化,氧气瓶9中氧气通过臭氧发生器8产生臭氧,该气体通过流量计进入臭氧氧化消毒器7内对其中降解后的水进行氧化消毒,调节臭氧浓度为40-100mg/L,反应时间为20min。氧化后的水经臭氧氧化消毒器7出水口自流存放到贮存池10,贮存池10设计水量调节器,当处理的水位到达设计水位时,贮存池10停止接收,当水位不足时,自来水自动补充。Take 2L each of kitchen cooking sewage, washing sewage, laundry sewage and bathing sewage, totaling 8L, pass through the stainless steel grid 1 with a gap of 2mm, remove larger solid particles, and enter the
其中,过滤器材料为石英砂;菌种为经培养、驯化后的降解表面活性剂和动植物油脂的优势降解菌;污水泵提水量6m3/h。微氧曝气滤池提水与充氧均采用上流式,空压机6充氧的氧气流速0.018m3/min,水力停留时间5.5h,反冲洗周期为20d。Among them, the filter material is quartz sand; the strains are cultivated and domesticated degrading surfactants and the dominant degrading bacteria of animal and vegetable oils; the water pumping capacity of the sewage pump is 6m 3 /h. The micro-aerobic aeration filter adopts the upflow type for water extraction and oxygenation. The oxygen flow rate of the
检测贮存池10的水质:CODcr 4.6mg/L,BOD5 1.6mg/L,总大肠杆菌2个/L,粪便大肠杆菌未检出,SS 2.1mg/L,pH7(参见表1)。并且处理后的再生水水质指标符合城市生活杂用水水质标准(GB-T18920-2002),完全可作为冲厕所用水,并且冲厕所后用水即可直接排入城市管网。Detect the water quality of the storage tank 10: CODcr 4.6mg/L, BOD 5 1.6mg/L,
表1Table 1
*城市生活杂用水水质标准(GB-T18920-2002)。*Water quality standard for urban miscellaneous water (GB-T18920-2002).
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100113974A CN101311131B (en) | 2007-05-23 | 2007-05-23 | Sewage handling method and uses thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2007100113974A CN101311131B (en) | 2007-05-23 | 2007-05-23 | Sewage handling method and uses thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101311131A true CN101311131A (en) | 2008-11-26 |
| CN101311131B CN101311131B (en) | 2010-06-23 |
Family
ID=40099988
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2007100113974A Expired - Fee Related CN101311131B (en) | 2007-05-23 | 2007-05-23 | Sewage handling method and uses thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101311131B (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101475258B (en) * | 2008-12-31 | 2010-12-22 | 南京中电联环保股份有限公司 | Bioactive coke method for processing coking wastewater |
| CN101519267B (en) * | 2009-04-14 | 2011-08-24 | 北京师范大学 | A combined treatment process for high-concentration organic wastewater |
| CN102249491A (en) * | 2011-06-16 | 2011-11-23 | 北京城市排水集团有限责任公司 | Deep treatment device and process for secondary treatment effluent of urban sewage plant |
| CN102260026A (en) * | 2011-06-29 | 2011-11-30 | 无锡强工机械工业有限公司 | Life miscellaneous wastewater biochemical treatment device |
| CN103212238A (en) * | 2012-01-19 | 2013-07-24 | 昆山思拓机器有限公司 | Water circulation system for laser wet-cutting system and filter paper strip replacement method therefor |
| CN105523624A (en) * | 2016-01-19 | 2016-04-27 | 天津大拇指环境工程有限公司 | Method and system for processing domestic wastewater of offshore oil drilling platforms |
| CN107601723A (en) * | 2017-10-31 | 2018-01-19 | 天津科艾福特科技有限公司 | A kind of wastewater treatment equipment |
| CN107746151A (en) * | 2017-10-27 | 2018-03-02 | 安徽中韩净化设备有限公司 | A kind of town domestic sewage purification process technique |
| CN107935314A (en) * | 2017-12-08 | 2018-04-20 | 广西永太和环保科技有限公司 | Soybean wastewater micro-organism treatment process |
| CN110229028A (en) * | 2019-07-17 | 2019-09-13 | 陕西天仁雪农业科技有限公司 | A kind of useless dish leaf processing method |
| CN110303029A (en) * | 2019-07-17 | 2019-10-08 | 陕西天仁雪农业科技有限公司 | A kind of food waste treatment device and processing method |
| CN110340109A (en) * | 2019-07-17 | 2019-10-18 | 陕西天仁雪农业科技有限公司 | A kind of discarded fruit processing method |
| CN110526487A (en) * | 2018-05-23 | 2019-12-03 | 河南仁华生物科技有限公司 | A kind of sewage treatment process |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1384066A (en) * | 2001-04-28 | 2002-12-11 | 沈阳碧水蓝天环境科技有限公司 | Biological reinforcer for treating domestic sewage and surface water |
| CN1278961C (en) * | 2004-02-16 | 2006-10-11 | 北京兰利东方科技有限公司 | Sewage treatment system for public lavatory |
| CN100429163C (en) * | 2005-09-12 | 2008-10-29 | 中国科学院生态环境研究中心 | Dispersed spot source sewage treating and grading reusing system and its operation process |
-
2007
- 2007-05-23 CN CN2007100113974A patent/CN101311131B/en not_active Expired - Fee Related
Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101475258B (en) * | 2008-12-31 | 2010-12-22 | 南京中电联环保股份有限公司 | Bioactive coke method for processing coking wastewater |
| CN101519267B (en) * | 2009-04-14 | 2011-08-24 | 北京师范大学 | A combined treatment process for high-concentration organic wastewater |
| CN102249491A (en) * | 2011-06-16 | 2011-11-23 | 北京城市排水集团有限责任公司 | Deep treatment device and process for secondary treatment effluent of urban sewage plant |
| CN102260026A (en) * | 2011-06-29 | 2011-11-30 | 无锡强工机械工业有限公司 | Life miscellaneous wastewater biochemical treatment device |
| CN102260026B (en) * | 2011-06-29 | 2013-02-13 | 无锡强工机械工业有限公司 | Life miscellaneous wastewater biochemical treatment device |
| CN103212238B (en) * | 2012-01-19 | 2015-12-02 | 昆山思拓机器有限公司 | Wet for laser the replacing options of water circulation system in cutting system and filter-paper-tape thereof |
| CN103212238A (en) * | 2012-01-19 | 2013-07-24 | 昆山思拓机器有限公司 | Water circulation system for laser wet-cutting system and filter paper strip replacement method therefor |
| CN105523624A (en) * | 2016-01-19 | 2016-04-27 | 天津大拇指环境工程有限公司 | Method and system for processing domestic wastewater of offshore oil drilling platforms |
| CN107746151A (en) * | 2017-10-27 | 2018-03-02 | 安徽中韩净化设备有限公司 | A kind of town domestic sewage purification process technique |
| CN107601723A (en) * | 2017-10-31 | 2018-01-19 | 天津科艾福特科技有限公司 | A kind of wastewater treatment equipment |
| CN107935314A (en) * | 2017-12-08 | 2018-04-20 | 广西永太和环保科技有限公司 | Soybean wastewater micro-organism treatment process |
| CN110526487A (en) * | 2018-05-23 | 2019-12-03 | 河南仁华生物科技有限公司 | A kind of sewage treatment process |
| CN110229028A (en) * | 2019-07-17 | 2019-09-13 | 陕西天仁雪农业科技有限公司 | A kind of useless dish leaf processing method |
| CN110303029A (en) * | 2019-07-17 | 2019-10-08 | 陕西天仁雪农业科技有限公司 | A kind of food waste treatment device and processing method |
| CN110340109A (en) * | 2019-07-17 | 2019-10-18 | 陕西天仁雪农业科技有限公司 | A kind of discarded fruit processing method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101311131B (en) | 2010-06-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101311131A (en) | Sewage handling method and uses thereof | |
| Ren et al. | Graywater treatment technologies and reuse of reclaimed water for toilet flushing | |
| CN201648174U (en) | An integrated gray water treatment unit | |
| CN102976548A (en) | Zero emission district sewage resource treatment apparatus | |
| CN206308215U (en) | A kind of integral domestic sewage treatment device | |
| CN203346230U (en) | Landfill leachate treatment device | |
| CN102211822A (en) | Method for comprehensively controlling black and odorous watercourse rivers and microbial inoculum drop irrigation device | |
| CN102718365A (en) | Buried sewage treatment device | |
| CN205398371U (en) | Rural miniaturized integration sewage treatment unit | |
| CN219603413U (en) | Circulating water flushing integrated ecological toilet system without sewer | |
| CN116534983B (en) | An ecological coupling system for efficiently treating rural gray water and its application | |
| CN101786092B (en) | A comprehensive treatment system and method for organic waste and domestic sewage | |
| CN101016186A (en) | Biological treatment method and device for ecological system of sewage circulation utilization | |
| CN1994935B (en) | Odor-free energy-saving micro aerobiont combined processing system for cabaret sewage processing and reusing | |
| CN111592141A (en) | Non-discharge self-cleaning type circulating water flushing toilet | |
| CN215627416U (en) | Garbage transfer station sewage treatment device | |
| CN101704621B (en) | An integrated gray water treatment method and system | |
| CN201473421U (en) | Buried sludge-free sewage integrated treatment device | |
| CN106517699A (en) | Efficient household garbage sewage system and technology thereof | |
| CN202499792U (en) | Device for treating toilet excrement by complete biological method | |
| CN116693047A (en) | Circulating water flushing sewer-free integrated ecological toilet system | |
| CN2641037Y (en) | Small life sewage treatment plant | |
| CN210915730U (en) | Toilet sewage purification equipment | |
| CN209456240U (en) | A kind of integration apparatus for sanitary sewage disposal | |
| CN201092555Y (en) | Efficient biological sewage treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100623 Termination date: 20110523 |
