CN114409193A - Resource type source separation modular toilet system and method for treating excrement by using same - Google Patents
Resource type source separation modular toilet system and method for treating excrement by using same Download PDFInfo
- Publication number
- CN114409193A CN114409193A CN202210073742.1A CN202210073742A CN114409193A CN 114409193 A CN114409193 A CN 114409193A CN 202210073742 A CN202210073742 A CN 202210073742A CN 114409193 A CN114409193 A CN 114409193A
- Authority
- CN
- China
- Prior art keywords
- module
- urine
- source separation
- resource
- feces
- 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
- 238000000926 separation method Methods 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 92
- 210000002700 urine Anatomy 0.000 claims abstract description 87
- 239000010802 sludge Substances 0.000 claims abstract description 40
- 238000004064 recycling Methods 0.000 claims abstract description 37
- 238000005352 clarification Methods 0.000 claims abstract description 26
- 210000003608 fece Anatomy 0.000 claims description 83
- 239000007788 liquid Substances 0.000 claims description 50
- 230000002550 fecal effect Effects 0.000 claims description 39
- 239000010865 sewage Substances 0.000 claims description 31
- 239000012528 membrane Substances 0.000 claims description 29
- 238000011010 flushing procedure Methods 0.000 claims description 26
- 239000010871 livestock manure Substances 0.000 claims description 25
- 238000004062 sedimentation Methods 0.000 claims description 23
- 238000003756 stirring Methods 0.000 claims description 22
- 238000005273 aeration Methods 0.000 claims description 20
- 238000005189 flocculation Methods 0.000 claims description 20
- 230000016615 flocculation Effects 0.000 claims description 20
- 238000010612 desalination reaction Methods 0.000 claims description 17
- 230000001954 sterilising effect Effects 0.000 claims description 17
- 239000012510 hollow fiber Substances 0.000 claims description 16
- 238000001556 precipitation Methods 0.000 claims description 16
- 238000004659 sterilization and disinfection Methods 0.000 claims description 13
- 238000000889 atomisation Methods 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims description 12
- 238000004332 deodorization Methods 0.000 claims description 11
- 239000005416 organic matter Substances 0.000 claims description 11
- 238000005485 electric heating Methods 0.000 claims description 10
- 229910052698 phosphorus Inorganic materials 0.000 claims description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 8
- 239000011574 phosphorus Substances 0.000 claims description 8
- 239000012141 concentrate Substances 0.000 claims description 7
- 238000001728 nano-filtration Methods 0.000 claims description 7
- 239000002245 particle Substances 0.000 claims description 7
- 238000010248 power generation Methods 0.000 claims description 7
- 239000003337 fertilizer Substances 0.000 claims description 6
- 150000003839 salts Chemical class 0.000 claims description 6
- 238000005115 demineralization Methods 0.000 claims description 5
- 230000002328 demineralizing effect Effects 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 230000001877 deodorizing effect Effects 0.000 claims description 4
- 230000027939 micturition Effects 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 3
- 238000011084 recovery Methods 0.000 claims 2
- 239000013589 supplement Substances 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 6
- 238000011033 desalting Methods 0.000 abstract 1
- 239000013049 sediment Substances 0.000 abstract 1
- 238000005192 partition Methods 0.000 description 10
- 238000010586 diagram Methods 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000000855 fermentation Methods 0.000 description 4
- 230000004151 fermentation Effects 0.000 description 4
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 4
- 235000019645 odor Nutrition 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 230000001580 bacterial effect Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002054 inoculum Substances 0.000 description 2
- 235000014655 lactic acid Nutrition 0.000 description 2
- 239000004310 lactic acid Substances 0.000 description 2
- 244000000010 microbial pathogen Species 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 230000032258 transport Effects 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000002781 deodorant agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012806 monitoring device Methods 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 238000001935 peptisation Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
- C05F3/04—Fertilisers from human or animal excrements, e.g. manure from human faecal masses
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
- C05F3/06—Apparatus for the manufacture
-
- E—FIXED CONSTRUCTIONS
- E04—BUILDING
- E04H—BUILDINGS OR LIKE STRUCTURES FOR PARTICULAR PURPOSES; SWIMMING OR SPLASH BATHS OR POOLS; MASTS; FENCING; TENTS OR CANOPIES, IN GENERAL
- E04H1/00—Buildings or groups of buildings for dwelling or office purposes; General layout, e.g. modular co-ordination or staggered storeys
- E04H1/12—Small buildings or other erections for limited occupation, erected in the open air or arranged in buildings, e.g. kiosks, waiting shelters for bus stops or for filling stations, roofs for railway platforms, watchmen's huts or dressing cubicles
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/302—Nitrification and denitrification treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
- C02F3/308—Biological phosphorus removal
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Architecture (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Structural Engineering (AREA)
- Civil Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Manufacturing & Machinery (AREA)
- Treatment Of Sludge (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明涉及厕所系统技术领域,尤其涉及一种资源型源分离模块化厕所系统及其处理粪污方法。The invention relates to the technical field of toilet systems, in particular to a resource-based source separation modular toilet system and a method for treating feces.
背景技术Background technique
人们日常生活中经常使用的为水冲厕所,常规水冲厕所每次冲厕使用5~8L 洁净水,随后冲厕水混合着尿液和粪便流入排水管网,最后流入污水处理厂进行污水处理。对于水资源缺乏地区,水冲厕所既浪费了水资源,也为后续污水处理带来了负担。研究资料表明,粪便和尿液体积仅占冲厕污水总量的1%~2%,但其却是冲厕污水中的主要污染负荷,其含碳量占总量的60%~70%,氮占总量的 90%以上,磷占总量的80%以上,钾占总量的60%~70%。People often use water to flush toilets in daily life. Conventional flush toilets use 5-8L of clean water for each flush, and then the flushing water mixed with urine and feces flows into the drainage pipe network, and finally flows into the sewage treatment plant for sewage treatment. . For water-deficient areas, flushing toilets not only wastes water resources, but also imposes a burden on subsequent sewage treatment. Research data show that the volume of feces and urine only accounts for 1% to 2% of the total flushing sewage, but they are the main pollution loads in the toilet flushing sewage, and their carbon content accounts for 60% to 70% of the total. Nitrogen accounts for more than 90% of the total, phosphorus accounts for more than 80% of the total, and potassium accounts for 60% to 70% of the total.
目前厕所的形式有连接进出水管网的固定式厕所以及整体式可以移动的活动厕所。对于固定式厕所而言,其占地面积大,建设成本高,埋设的地下管网容易受到其他管网的影响,且冲厕水增大污水处理厂的污染负荷;对于可以移动的活动厕所其各个设备实现整体化,不方便搬运和安装,不能根据客流量对厕所的数量进行调整。At present, toilets are in the form of fixed toilets connected to the water inlet and outlet network and integral movable toilets. For fixed toilets, it occupies a large area, and the construction cost is high. The buried underground pipe network is easily affected by other pipe networks, and the flushing water increases the pollution load of the sewage treatment plant; for movable toilets, its All equipment is integrated, which is inconvenient for handling and installation, and the number of toilets cannot be adjusted according to passenger flow.
发明内容SUMMARY OF THE INVENTION
发明目的:本发明的目的提供一种高效源分离与污染处理、节能、绿色环保的资源型源分离模块化厕所系统;本发明的另一目的是提供一种利用资源型源分离模块化厕所系统处理粪污方法。Purpose of the invention: The purpose of the present invention is to provide a resource-based source separation modular toilet system with efficient source separation and pollution treatment, energy saving, and environmental protection; another purpose of the present invention is to provide a resource-based source separation modular toilet system. Methods of handling manure.
技术方案:本发明的资源型源分离模块化厕所系统,包括采用榫卯结构组装并依次相连的粪尿源分离单元,尿液处理和循环利用单元,用于粪便有机肥发酵的粪便好氧腐殖资源化单元;粪尿源分离单元包括尿液收集区和粪便收集区;尿液处理和循环利用单元包括与粪便收集区连接澄清模块,澄清模块连接有与尿液收集区连接的多效资源化模块,多效处理模块连接有沉淀、污泥回流模块及除盐模块,其中沉淀、污泥回流模块与除盐模块相连,除盐模块连接有储水回用模块,储水回用模块与粪尿源分离单元连接。Technical scheme: The resource-based source separation modular toilet system of the present invention includes a feces and urine source separation unit assembled and connected in sequence with a tenon-and-mortise structure, a urine treatment and recycling unit, and a fecal aerobic rot for fecal organic fertilizer fermentation. Reproduction unit; feces and urine source separation unit includes urine collection area and feces collection area; urine treatment and recycling unit includes clarification module connected with feces collection area, clarification module is connected with multi-effect resources connected with urine collection area The multi-effect treatment module is connected with a sedimentation, sludge return module and a desalination module, wherein the sedimentation and sludge return module is connected with the desalination module, the desalination module is connected with a water storage and reuse module, and the water storage and reuse module is connected with The urine source separation unit is connected.
本发明将厕所设置成模块化,可以在工厂预制,现场组装,减少了搬运的劳动力,可根据客流量变化对厕所的数量进行增加或减少,采用榫卯结构,通过构件之间的穿插组合,将各构件牢牢契合在一起,无需繁复的装搬工艺,让构件与实际功能相结合。The invention sets the toilet into a modular structure, which can be prefabricated in the factory and assembled on site, which reduces the labor for handling, and can increase or decrease the number of toilets according to the change of passenger flow. Firmly fit the components together, without the need for complicated loading and handling processes, so that the components can be combined with the actual function.
进一步地,还包括用于为系统提供电能补充的可持续能源利用单元,可持续能源利用单元包括太阳能发电板、风车、蓄电池组和离网型逆变控制器,其中发电板和风车分别与蓄电池组电连,蓄电池组与离网型逆变控制器电连。Further, it also includes a sustainable energy utilization unit for supplying electric power to the system, and the sustainable energy utilization unit includes a solar power generation panel, a windmill, a battery pack and an off-grid inverter controller, wherein the power generation panel and the windmill are respectively connected with the storage battery. The battery pack is electrically connected with the off-grid inverter controller.
进一步地,粪尿源分离单元包括便池,便池的后端设有冲厕口,便池的前端设有将便池分为尿液收集区和粪便收集区的挡板;在尿液收集区设有集尿口,集尿口底部连通有排尿管;在粪便收集区的便池底部开设有一孔洞,孔洞与弯管连接,弯管上设有用于粉碎固体物质的粉碎切割式污水提升泵。Further, the feces and urine source separation unit includes a urinal, the rear end of the urinal is provided with a flushing port, and the front end of the urinal is provided with a baffle that divides the urinal into a urine collection area and a feces collection area; There is a urine collection port in the area, and the bottom of the urine collection port is connected with a urination pipe; there is a hole at the bottom of the urinal in the feces collection area, and the hole is connected with an elbow, and the elbow is provided with a crushing and cutting sewage lifting pump for crushing solid substances. .
进一步地,澄清模块包括与粪尿源分离单元中粪便收集区连通的多格式搅拌絮凝澄清池,多格式搅拌絮凝澄清池上部设有环形挡板,下部设有与环形挡板连接的三角形环形挡板,多格式搅拌絮凝澄清池的顶部设有自动加药机、用于搅拌的电机和第一雾化除臭杀菌机;电机与搅拌桨电连,搅拌桨设在三角形环形挡板围设的区域内;自动加药机分别与第一加药管和第二加药管连接,第一加药管伸入环形挡板围设的区域内,第二加药管伸入三角形环形挡板围设的区域内。Further, the clarification module includes a multi-format stirring flocculation clarifier connected with the feces collection area in the feces and urine source separation unit, the upper part of the multi-format stirring flocculation clarifier is provided with an annular baffle, and the lower part is provided with a triangular annular baffle connected with the annular baffle. The top of the multi-format stirring flocculation clarifier is equipped with an automatic dosing machine, a motor for stirring and the first atomization deodorization and sterilization machine; the motor is electrically connected with the stirring paddle, and the stirring paddle is arranged in the triangular annular baffle. The automatic dosing machine is connected with the first dosing tube and the second dosing tube respectively, the first dosing tube extends into the area enclosed by the annular baffle, and the second dosing tube extends into the triangular annular baffle enclosure within the set area.
进一步地,多效资源化模块包括分别与澄清模块、粪尿源分离单元中的尿液收集区连通的粪污液体多效处理池,粪污液体多效处理池内设有中空纤维膜,中空纤维膜连接有离心式管道风机,离心式管道风机用于向中空纤维膜内部运输低压进行无泡曝气,中空纤维膜的底部设有曝气头,曝气头依次连接有反冲洗管和回转式鼓风机;粪污液体多效处理池的顶部设有第二雾化除臭杀菌机。Further, the multi-effect recycling module includes a multi-effect treatment tank for feces liquid which is respectively connected with the clarification module and the urine collection area in the feces and urine source separation unit. The membrane is connected with a centrifugal duct fan. The centrifugal duct fan is used to transport low pressure to the inside of the hollow fiber membrane for bubble-free aeration. The bottom of the hollow fiber membrane is provided with an aeration head. The aeration head is sequentially connected with a backwash pipe and a rotary type. Blower; the top of the multi-effect treatment tank for manure liquid is provided with a second atomization deodorization and sterilization machine.
进一步地,沉淀、污泥回流模块包括与多效资源化模块连接的沉淀池,沉淀池连接有污泥回流泵,污泥回流泵与多效处理池连接。Further, the sedimentation and sludge return module includes a sedimentation tank connected with the multi-effect recycling module, the sedimentation tank is connected with a sludge return pump, and the sludge return pump is connected with the multi-effect treatment tank.
进一步地,除盐模块包括用于除盐的纳滤膜组件,用于将沉淀、污泥回流模块中的水抽提至除盐模块中的加压泵。Further, the demineralization module includes a nanofiltration membrane module for demineralization, and a pressurized pump for extracting water in the sedimentation and sludge return modules to the demineralization module.
进一步地,储水回用模块包括储水回用池,储水回用池上方设有与除盐模块连接管道式紫外线消毒器,储水回用池依次连接有提升泵和冲水管,冲水管与粪尿源分离单元连接。Further, the water storage and reuse module includes a water storage and reuse pool, a pipeline-type ultraviolet sterilizer connected to the desalination module is arranged above the water storage and reuse pool, and a lift pump and a flushing pipe are sequentially connected to the water storage and reuse pool. Connect to the fecal and urine source separation unit.
进一步地,粪便好氧腐殖资源化单元包括与澄清模块连接的粪便腐殖化池和用于提供热源的电热炉,粪便腐殖化池的底部设有湿度传感器,湿度传感器与电热炉电连,粪便腐殖化池内设有生物腐殖化菌剂箱和第三雾化除臭杀菌机。Further, the fecal aerobic humification recycling unit includes a fecal humification pond connected with the clarification module and an electric heating furnace for providing a heat source. A humidity sensor is provided at the bottom of the fecal humification pond, and the humidity sensor is electrically connected to the electric heating furnace. , The fecal humification tank is equipped with a biological humification agent box and a third atomization deodorization and sterilization machine.
另一方面,本发明的利用上述的资源型源分离模块化厕所系统处理粪污方法,包括以下步骤:On the other hand, the present invention utilizes the above-mentioned resource-based source separation modular toilet system to process manure, comprising the following steps:
(1)粪尿源分离单元分别收集粪便和尿液;(1) The feces and urine source separation unit collects feces and urine respectively;
粪便经由粉碎切割式污水提升泵进入澄清模块进行絮凝澄清,经过絮凝处理的大颗粒絮凝体排至粪便好氧腐殖资源化单元,处理后的污水流入多效资源化模块;其中絮凝剂为聚丙烯酰胺;The feces enter the clarification module through the crushing and cutting sewage lifting pump for flocculation and clarification. The large particle flocs after flocculation are discharged to the fecal aerobic humification recycling unit, and the treated sewage flows into the multi-effect recycling module; the flocculant is polymer Acrylamide;
尿液直接排至多效资源化模块;Urine is directly discharged to the multi-effect resource module;
(2)多效资源化模块接收污水和尿液,进行无泡曝气,其中中空纤维膜上附着的生物膜由内向外形成好氧层、缺氧层和厌氧层,实现尿液的硝化和反硝化反应,降解粪污液体中的有机物,并完成脱氮除磷,处理后的粪污液体进入沉淀、污泥回流模块;(2) The multi-effect resource recycling module receives sewage and urine, and performs bubble-free aeration. The biofilm attached to the hollow fiber membrane forms an aerobic layer, an anoxic layer and an anaerobic layer from the inside to the outside to realize the nitrification of urine. Reacts with denitrification, degrades the organic matter in the manure liquid, and completes denitrification and phosphorus removal, and the treated manure liquid enters the sedimentation and sludge return module;
沉淀、污泥回流模块接收粪污液体进行沉淀,沉淀得到的污泥回流至多效资源化模块中回用,沉淀后清水进入除盐模块进行处理;The precipitation and sludge return module receives the fecal liquid for precipitation, the sludge obtained by precipitation is returned to the multi-effect resource recycling module for reuse, and the clean water enters the desalination module for treatment after precipitation;
除盐模块去沉淀后清水中的盐分、有机物和色度,得到高浓度浓缩液和出水,高浓度浓缩液回流至多效资源化模块进行处理;出水流入储水回用模块进行杀菌处理,杀菌后的纯水储存在储水回用池中,储水回用池中的纯水流入粪尿源分离单元进行冲厕;The desalination module removes the salt, organic matter and chromaticity in the clean water after precipitation to obtain high-concentration concentrate and effluent. The high-concentration concentrate is returned to the multi-effect recycling module for treatment; the effluent flows into the water storage and reuse module for sterilization treatment. The pure water is stored in the water storage and reuse pool, and the pure water in the water storage and reuse pool flows into the feces and urine source separation unit for toilet flushing;
(3)粪便好氧腐殖资源化单元接收澄清模块流出的大颗粒絮凝体干燥至含水率为40%~60%,然后进行生物腐殖化制作有机肥料;其中发酵菌剂采用乳酸菌:芽孢菌:酵母菌含量1:1:1的混合型发酵菌剂。(3) The fecal aerobic humification recycling unit receives the large-particle flocs from the clarification module and dries to a moisture content of 40% to 60%, and then conducts biological humification to make organic fertilizers; wherein the fermentation inoculum adopts lactic acid bacteria: Bacillus : Mixed fermentation inoculum with 1:1:1 yeast content.
本发明针对此问题,提出一种可以对粪尿进行源分离与污染处理的厕所,不仅可以降低粪污的污染负荷,同时还可实现粪污的资源化可持续利用。Aiming at this problem, the present invention proposes a toilet capable of source separation and pollution treatment of feces and urine, which can not only reduce the pollution load of feces, but also realize the sustainable utilization of feces as resources.
有益效果:与现有技术相比,本发明具有如下显著优点:(1)有效降低粪污的污染负荷提高处理效率:采用源分离技术,在源头将尿液和掺杂着粪便的冲厕水分离,再对两者分别进行处理,尿液排至粪污液体处理单元进行有机物以及氮磷的去除,掺杂着粪便的冲厕水经过固液分离,将脱水的粪便进行发酵制肥,冲厕水通过粪污液体处理单元从而进行循环冲厕,通过源分离技术,将尿液和粪污液体单独处理,减少粪污液体的污染程度,实现各自的高效处理,提高资源利用率;Beneficial effects: Compared with the prior art, the present invention has the following significant advantages: (1) effectively reducing the pollution load of feces and improving treatment efficiency: using source separation technology, urine and toilet flushing water mixed with feces are separated at the source Separate, and then treat the two separately. The urine is discharged to the fecal liquid treatment unit to remove organic matter and nitrogen and phosphorus. The toilet flushing water mixed with feces is separated from solid and liquid, and the dehydrated feces are fermented to make fertilizer and flushed. The toilet water is circulated through the fecal liquid treatment unit to flush the toilet, and through the source separation technology, the urine and the fecal liquid are treated separately to reduce the pollution degree of the fecal liquid, realize their efficient treatment, and improve the resource utilization rate;
(2)安装方便:将各个处理单元进行模块化,采用榫卯结构将各个处理模块进行组装,模块化厕所减少了大量的劳动力,与传统的厕所相比,模块化厕所减少了大量的劳动力,施工周期缩短50%以上,原材料使用上减少80%,建筑物垃圾减少70%以上,模块化厕所方便加工,在工厂即可预制,现场组装,方便工人的搬运;模块化厕所方便检查设备运行情况,当某个组件出现故障时,可以随时查看出故障的设备;(2) Easy installation: modularize each processing unit and assemble each processing module with a tenon-and-mortise structure. The modular toilet reduces a lot of labor. Compared with the traditional toilet, the modular toilet reduces a lot of labor. The construction period is shortened by more than 50%, the use of raw materials is reduced by 80%, and the construction waste is reduced by more than 70%. The modular toilet is easy to process and can be prefabricated in the factory and assembled on site, which is convenient for workers to carry; the modular toilet is convenient to check the operation of the equipment , when a component fails, you can view the faulty equipment at any time;
(3)节能且绿色环保:由于尿液中的COD以及N、P含量很高,通过膜曝气生物反应技术与活性污泥法相结合的新型、高效污水处理技术,通过无泡曝气这种高效的氧利用率方式、内外分层的特殊生物膜结构再结合活性污泥法,从而实现污水的脱氮除磷以及大量有机物的去除;无泡曝气技术的曝气动力效率可达到10kgO2/kwh,在适宜条件下甚至可以达到14kgO2/kwh,这个数值是传统曝气形式的3-4倍,相应而言几乎能够节约75%的曝气电耗。(3) Energy saving and green environmental protection: Due to the high content of COD and N and P in urine, a new and efficient sewage treatment technology combining membrane aeration biological reaction technology and activated sludge method, through bubble-free aeration, Efficient oxygen utilization method, special biofilm structure of internal and external layers combined with activated sludge method, so as to achieve denitrification and phosphorus removal of sewage and removal of a large amount of organic matter; the aeration power efficiency of bubble-free aeration technology can reach 10kgO 2 /kwh, under suitable conditions, it can even reach 14kgO 2 /kwh, which is 3-4 times that of the traditional aeration form, and correspondingly, it can save almost 75% of the aeration power consumption.
附图说明Description of drawings
图1为本发明的总平面布置示意图;Fig. 1 is the general plan layout schematic diagram of the present invention;
图2为本发明的内部结构示意图;Fig. 2 is the internal structure schematic diagram of the present invention;
图3为粪尿源分离单元结构示意图;Fig. 3 is the excrement and urine source separation unit structural representation;
图4为澄清模块结构示意图;Figure 4 is a schematic structural diagram of a clarification module;
图5为多效资源化模块结构示意图;5 is a schematic structural diagram of a multi-effect resourceization module;
图6为沉淀、污泥回流模块及除盐模块结构示意图;FIG. 6 is a schematic structural diagram of a sedimentation, sludge return module and a desalination module;
图7为储水回用模块结构示意图;7 is a schematic structural diagram of a water storage and reuse module;
图8为粪便好氧腐殖资源化单元结构示意图;Fig. 8 is a schematic diagram of the structure of a fecal aerobic humification resource utilization unit;
图9为可持续能源利用单元结构示意图。Figure 9 is a schematic diagram of the structure of a sustainable energy utilization unit.
具体实施方式Detailed ways
下面结合附图对本发明的技术方案作进一步说明。The technical solutions of the present invention will be further described below with reference to the accompanying drawings.
1、粪尿源分离单元;101、便池;102、挡板;103、集尿口;104、排尿管; 105、粉碎切割式污水提升泵;106、冲厕口;107、地下设备间;2、尿液处理和循环利用单元;201、多格式搅拌絮凝澄清池;202、自动加药机;203、电机; 204、进水管;205、第一隔板;206、搅拌桨;207、三角形环形挡板;208、环形挡板;209、第一加药管;210、第二加药管;211、排渣管;212、排水槽;213、排水管;214、中空纤维膜;215、支架;216、离心式管道风机;217、单向阀; 218、进气管;219、回转式鼓风机;220、电动阀门;221、曝气头;222、粪污液体多效处理池;223、反冲洗管;224、粪污液体排水管;225、污泥回流泵; 226、沉淀池;227、污泥回流管;228、管道式紫外线消毒器;229、纯水出水管; 230、储水回用池;231、提升泵;232、冲水管;233、加压泵;234、纳滤膜组件;235、第二隔板;236、进水口;237、出水口;238、钢架;239、出水管;240、浓缩液排出管;241、第三隔板;242、第一雾化除臭杀菌机;243、第二雾化除臭杀菌机;244、液位控制计;3、粪便好氧腐殖资源化单元;301、粪便腐殖化池;302、湿度传感器;303、电热炉;304、冷气进气口;305、热气出气口; 306、生物腐殖化菌剂箱;307、投加管;308、菌剂喷洒头;309、第四隔板;310、第三雾化除臭杀菌机;4、可持续能源利用单元;401、太阳能发电板;402、风车;403、蓄电池组;404、离网型逆变控制器;405、设备间。1. Excrement and urine source separation unit; 101, urinal; 102, baffle; 103, urine collecting port; 104, urination pipe; 105, crushing and cutting sewage lifting pump; 106, toilet flushing port; 107, underground equipment room; 2. Urine treatment and recycling unit; 201, multi-format stirring flocculation clarifier; 202, automatic dosing machine; 203, motor; 204, water inlet pipe; 205, first partition; 206, stirring paddle; 207, triangle Annular baffle; 208, annular baffle; 209, first dosing pipe; 210, second dosing pipe; 211, slag discharge pipe; 212, drainage groove; 213, drainage pipe; 214, hollow fiber membrane; 215, Bracket; 216, Centrifugal duct fan; 217, Check valve; 218, Intake pipe; 219, Rotary blower; 220, Electric valve; 221, Aeration head; 222, Multi-effect treatment tank for manure liquid; 223, Reverse Rinse pipe; 224, manure liquid drainage pipe; 225, sludge return pump; 226, sedimentation tank; 227, sludge return pipe; 228, pipeline type ultraviolet sterilizer; 229, pure water outlet pipe; 230, water storage return pipe Use pool; 231, lift pump; 232, flushing pipe; 233, pressurized pump; 234, nanofiltration membrane module; 235, second partition plate; 236, water inlet; 237, water outlet; 238, steel frame; 239, Water outlet pipe; 240, concentrate discharge pipe; 241, third partition plate; 242, first atomization deodorization and sterilization machine; 243, second atomization deodorization and sterilization machine; 244, liquid level controller; 3, good feces Oxygen humification recycling unit; 301, fecal humification tank; 302, humidity sensor; 303, electric heating furnace; 304, cold air inlet; 305, hot air outlet; 306, biological humification agent box; 307, Dosing pipe; 308, bacterial agent spray head; 309, fourth partition; 310, third atomization deodorization and sterilization machine; 4, sustainable energy utilization unit; 401, solar power panel; 402, windmill; 403, battery group; 404, off-grid inverter controller; 405, equipment room.
如图1-9所示,一种资源型源分离模块化厕所包括粪尿源分离单元1、尿液处理和循环利用单元2、粪便好氧腐殖资源化单元3、可持续能源利用单元4。As shown in Figures 1-9, a resource-based source separation modular toilet includes a feces and urine
其中,所述的粪尿源分离单元1,包括尿液收集区和粪便收集区;以其中一个具体说明,包括便池101,粉碎切割式污水提升泵105;在便池101前端设置 20cm的挡板102,挡板102将便池101分为尿液收集区和粪便收集区;尿液收集区开孔,孔径为DN10mm,下端设置集尿口103进行尿液收集,排尿管104 与集尿口103连接进行尿液输送;粪便收集区中的粪便和冲厕水无法通过重力作用自然排放至多格式搅拌絮凝澄清池201,在地下设备间107设置可以一次性最大提升20~32L粪污液体的粉碎切割式污水提升泵105,泵入口处的切割器将含粪便、卫生纸等固体物质打碎,再提升至多格式搅拌絮凝澄清池201;在便池101 后端设置冲厕口106;粪尿源分离单元1在源头上将尿液和掺杂粪便的冲厕水进行分离,两者各自进行高效处理。Among them, the feces and urine
所述的尿液处理和循环利用单元2包括澄清模块、多效资源化模块、沉淀、污泥回流模块、除盐模块与储水回用模块。The urine treatment and
其中,所述的澄清模块包括多格式搅拌絮凝澄清池201,自动加药机202,用于搅拌的电机203,第一雾化除臭杀菌机242;池右侧开口连接进水管204,自动加药机202和电机203放置在第一隔板205上,第一隔板中间开口,电机 203与搅拌桨206连接,带动搅拌桨206工作,池下部设置三角形环形挡板207,挡板开口角度为45°,三角形环形挡板207与搅拌桨206下部之间的区域为第一絮凝室,与三角形环形挡板207相连的为环形挡板208,环形挡板208内部区域为第二絮凝室,挡板上设置大小均匀的开口;通过自动加药机202向池中定量投加絮凝剂聚丙烯酰胺,自动加药机202连接两根加药管,第一加药管209与第二加药管210分别投加至第一絮凝室和第二絮凝室;进水管204下方区域为污泥浓缩区,经过絮凝处理的大颗粒絮凝体通过排渣管211排至粪便腐殖化池301,处理后的污水漂浮至水面,流进排水槽212由排水管213排至粪污液体多效处理池222;池顶部由支架连接第一雾化除臭杀菌机242,雾化除臭杀菌机将除臭菌剂喷洒于整个空间,除臭菌剂与臭气在池内反应,以此来除臭,喷洒方式为雾化方式,因此雾化除臭杀菌机做的小,方便安装。Among them, the clarification module includes a multi-format stirring
所述的多效资源化模块包括粪污液体多效处理池222,中空纤维膜214,支架215,离心式管道风机216,单向阀217,进气管218,回转式鼓风机219,电动阀门220,曝气头221;第二雾化除臭杀菌机243;中空纤维膜214安装在支架215上,支架215固定在粪污液体多效处理池222顶部,中空纤维膜214与离心式管道风机216的进气管218连接,离心式管道风机216向中空纤维膜214 内部运输低压,进行无泡曝气,进气管218上设置单向阀217控制气体流向,离心式管道风机216放置在地下设备间107,地下设备间107两侧设置通风口;离心式管道风机216采用GDF1.4-8型号,其输送压力小45Pa,电机功率低0.003KW,噪声小38dB,重量轻4Kg;曝气头221设置在中空纤维膜214底部,回转式鼓风机219通过反冲洗管223与曝气头221连接,反冲洗管223上设置电动阀门,自动控制的回转式鼓风机219向池中曝气,回转式鼓风机219进行高强度短时冲刷,去除中空纤维膜214表面的生物膜,提高粪污液体处理性能;粪污液体多效处理池222右侧连接多格式搅拌絮凝澄清池201的排水管213进水,左侧设置粪污液体排水管224将处理好的粪污液体排出;此设备氧气由中空纤维膜214膜腔内向膜外扩散,氧气进气方向与污水进水方向相反,因此在中空纤维膜214上附着的生物膜由内向外形成好氧层、缺氧层和厌氧层,实现尿液的硝化和反硝化反应,降解粪污液体中的有机物,并完成脱氮除磷,在粪污液体多效处理池222 顶部设置第二雾化除臭杀菌机243,以此来去除池内的病原性微生物以及臭气;池下部开孔,粪尿源分离单元的排尿管104与孔口连接,尿液由此进入粪污液体多效处理池222进行粪污液体处理。The multi-effect recycling module includes a manure liquid
所述的沉淀、污泥回流模块位于下半部分包括沉淀池226和污泥回流泵225;处理后的粪污液体从池右侧的粪污液体排水管224流入,在沉淀池226进行沉淀,在沉淀池226底部形成分层,上部为清水层,下部为活性污泥层,在活性污泥层设置污泥回流泵225,污泥回流泵225通过污泥回流管227将污泥回流至粪污液体多效处理池222,清水层的水通过沉淀池226上部的管道排至加压泵233进水口236;多效资源化模块和沉淀、污泥回流模块结合活性污泥法和生物膜法,可以降解水中的有机物以及氮磷,提高处理效率。The described precipitation and sludge return module is located in the lower half and includes a
所述的除盐模块包括加压泵233以及纳滤膜组件234;加压泵233设置在第二隔板235上,加压泵233左侧为进水口236,右侧为出水口237,纳滤膜组件 234由钢架238支撑,纳滤膜组件234右侧进水,经过膜处理后从左侧出水管239 排至管道式紫外线消毒器228的进水口,纳滤膜组件234左上部为浓缩液排出管 240,浓缩液排出管240将处理完之后产生的高浓度浓缩液重新排至粪污液体多效处理池222;纳滤生物膜可以去除粪污液体中有机物和色度,降低粪污液体的硬度,高效率去除尿液中的盐分。The desalination module includes a
所述的储水回用模块包括管道式紫外线消毒器228,管道式紫外线消毒器 228放置在储水回用池230上部的第三隔板241上,管道式紫外线消毒器228右侧为进水口,连接出水管239;左侧为出水口,连接纯水出水管229,纯水出水管229将经过管道式紫外线消毒器228消毒后的纯水排至储水回用池230,采用型号为ZXB-RD150的管道式紫外线消毒器,额定流量1.7-2.2L/S,功率为150w,外壳尺寸直径×长度为102×1610mm,进出水管DN50,病毒、细菌的除去率可达到99.99%以上,杀菌快,没有任何副作用,不改变水的物理性质、化学性质;提升泵231设置在地下设备间107,纯水通过与提升泵231连接的冲水管232进入冲厕口106进行冲厕,在储水回用池230内壁上设置液位控制计244,根据需水量对液位进行自动控制,当储水回用池230内的水位低于液位控制计244的最低要求水位时,提升泵231立即停止工作,当液位回升至液位控制计244的安全水位时,提升泵231启动工作;尿液处理和循环利用单元2是将尿液和固液分离后的冲厕水进行污染物去除,包括尿液中的高含盐量以及冲厕水中的COD、N、 P、SS、色度、臭味的有效去除,将处理后的水进行回用,实现水的资源化利用;尿液处理和循环利用单元2是由多个模块组合而成,占地面积小,处理过程方便,可以及时检查处理运行情况以及药剂的使用量。The described water storage and reuse module includes a pipeline type
所述的粪便好氧腐殖资源化单元3,包括粪便腐殖化池301,电热炉303,生物腐殖化菌剂箱306,第三雾化除臭杀菌机310;经过多格式搅拌絮凝澄清池 201处理后的排放污泥通过排渣管211排至粪便腐殖化池301,其含水率过高为 98%左右,将污泥进行发酵需污泥含水率为40%~60%,含水率过高使空气含量下降,堆温下降,形成发臭的中间产物;在池底部设置湿度传感器302,对排放污泥进行水量检测;地下设备间107设置电热炉303,电热炉303右侧为冷气进气口304,电热炉303上部为热气出气口305;湿度传感器302通过监测装置控制电热炉303的运行;池顶部设置第四隔板309,生物腐殖化菌剂箱306放置在隔板上,投加管307与生物腐殖化菌剂箱306连接,投加管307底部安装菌剂喷洒头308,发酵菌剂采用乳酸菌:芽孢菌:酵母菌含量1:1:1的混合型发酵菌剂,将粪便进行生物腐殖化制作有机肥料,实现粪便的资源化处理;在粪便腐殖化池301的侧壁上设置第三雾化除臭杀菌机310,去除池内的病原性微生物以及臭气;粪便好氧腐殖资源化单元3对固液分离后的粪便进行有机肥的发酵,实现粪便的资源化利用。The fecal aerobic humification
所述的可持续能源利用单元4包括可持续能源接收装置:太阳能发电板401 以及风车402,蓄电池组403,离网型逆变控制器404;由光敏材料制作的太阳能发电板401和风车402放置在屋顶上方,以便于接受太阳光和风能;蓄电池组 403和离网型逆变控制器404放置在设备间,蓄电池组403将接受的电能储存起来,由离网型逆变控制器404将直流电转化为交流电,为厕所的电灯以及厕所的污水、粪便处理单元的各项设备如粉碎切割式污水提升泵105、电机203、回转式鼓风机219等处理设备提供电能;由于厕所占地面积有限,太阳能发电板401 和风车402设计规模较小,此模块产生的电能较少,将此模块产生的电能作为整体设备需电的电能补充,由此可以减少一些电量。The sustainable
利用上述的资源型源分离模块化厕所系统处理粪污方法,包括以下步骤:Utilize the above-mentioned resource-based source separation modular toilet system to treat manure, including the following steps:
(1)粪尿源分离单元分别收集粪便和尿液;(1) The feces and urine source separation unit collects feces and urine respectively;
粪便经由粉碎切割式污水提升泵进入澄清模块进行去絮凝澄清,絮凝剂为聚丙烯酰胺,经过絮凝处理的大颗粒絮凝体排至粪便好氧腐殖资源化单元,处理后的污水流入多效资源化模块;尿液直接排至多效资源化模块;The feces enter the clarification module through the crushing and cutting sewage lifting pump for deflocculation and clarification. The flocculant is polyacrylamide. The large particle flocs after flocculation treatment are discharged to the fecal aerobic humification recycling unit, and the treated sewage flows into multi-effect resources. chemical module; urine is directly discharged to the multi-effect recycling module;
(2)多效资源化模块接收污水和尿液,进行无泡曝气,其中中空纤维膜上附着的生物膜由内向外形成好氧层、缺氧层和厌氧层,实现尿液的硝化和反硝化反应,降解粪污液体中的有机物,并完成脱氮除磷,处理后的粪污液体进入沉淀、污泥回流模块;(2) The multi-effect resource recycling module receives sewage and urine, and performs bubble-free aeration. The biofilm attached to the hollow fiber membrane forms an aerobic layer, an anoxic layer and an anaerobic layer from the inside to the outside to realize the nitrification of urine. Reacts with denitrification, degrades the organic matter in the manure liquid, and completes denitrification and phosphorus removal, and the treated manure liquid enters the sedimentation and sludge return module;
沉淀、污泥回流模块接收粪污液体进行沉淀,沉淀得到的污泥回流至多效资源化模块中回用,沉淀后清水进入除盐模块进行处理;The precipitation and sludge return module receives the fecal liquid for precipitation, the sludge obtained by precipitation is returned to the multi-effect resource recycling module for reuse, and the clean water enters the desalination module for treatment after precipitation;
除盐模块去沉淀后清水中的盐分、有机物和色度,得到高浓度浓缩液和出水,高浓度浓缩液回流至多效资源化模块进行处理;出水流入储水回用模块进行杀菌处理,杀菌后的纯水储存在储水回用池中,储水回用池中的纯水流入粪尿源分离单元进行冲厕;The desalination module removes the salt, organic matter and chromaticity in the clean water after precipitation to obtain high-concentration concentrate and effluent. The high-concentration concentrate is returned to the multi-effect recycling module for treatment; the effluent flows into the water storage and reuse module for sterilization treatment. The pure water is stored in the water storage and reuse pool, and the pure water in the water storage and reuse pool flows into the feces and urine source separation unit for toilet flushing;
(3)粪便好氧腐殖资源化单元接收澄清模块流出的大颗粒絮凝体干燥至含水率为40%~60%,然后进行生物腐殖化制作有机肥料。(3) The fecal aerobic humification resourceization unit receives the large-particle flocs flowing out of the clarification module and dries to a moisture content of 40% to 60%, and then conducts biological humification to make organic fertilizers.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210073742.1A CN114409193B (en) | 2022-01-21 | 2022-01-21 | Resource type source separation modularized toilet system and method for treating feces by using same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210073742.1A CN114409193B (en) | 2022-01-21 | 2022-01-21 | Resource type source separation modularized toilet system and method for treating feces by using same |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114409193A true CN114409193A (en) | 2022-04-29 |
| CN114409193B CN114409193B (en) | 2023-05-02 |
Family
ID=81275952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210073742.1A Active CN114409193B (en) | 2022-01-21 | 2022-01-21 | Resource type source separation modularized toilet system and method for treating feces by using same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114409193B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115090119A (en) * | 2022-06-14 | 2022-09-23 | 北京建筑大学 | Urine-excrement-flushing water in-situ separation treatment system |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1086929A1 (en) * | 1999-08-02 | 2001-03-28 | NOPA Ltd. | Process for recycling water in a at least partially closed water cycle |
| CN101638909A (en) * | 2009-08-13 | 2010-02-03 | 宁波市江北怡宁环保科技有限公司 | Green ecotypical toilet |
| US20120018374A1 (en) * | 2009-04-09 | 2012-01-26 | Youfeng Sun | Sewage Treatment Process and System |
| CN106587538A (en) * | 2017-01-10 | 2017-04-26 | 上海应用技术大学 | Method for treating excrement and urine wastes |
| WO2018066443A1 (en) * | 2016-10-03 | 2018-04-12 | 誠一 金 | Dirty wastewater purification system |
| CN207412108U (en) * | 2017-05-16 | 2018-05-29 | 西安建筑科技大学 | A stool and urine separation toilet |
| CN108609814A (en) * | 2018-07-03 | 2018-10-02 | 夏海宗 | Toilet fecaluria recycling treatment equipment |
| CN109319897A (en) * | 2018-11-07 | 2019-02-12 | 中石化石油工程技术服务有限公司 | Co-direction stratified clarification and dehardening device for anti-fouling of heat exchange tube wall of evaporative desalination equipment |
| CN110241901A (en) * | 2019-06-25 | 2019-09-17 | 周鼎力 | A kind of environment-friendly type lavatory vehicle |
| CN112939649A (en) * | 2021-02-01 | 2021-06-11 | 北京建筑大学 | Integrated integrated wet garbage in-situ recycling treatment system and treatment method |
| CN113480009A (en) * | 2021-08-23 | 2021-10-08 | 浙江开创环保科技股份有限公司 | Membrane aeration sewage treatment system |
-
2022
- 2022-01-21 CN CN202210073742.1A patent/CN114409193B/en active Active
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1086929A1 (en) * | 1999-08-02 | 2001-03-28 | NOPA Ltd. | Process for recycling water in a at least partially closed water cycle |
| US20120018374A1 (en) * | 2009-04-09 | 2012-01-26 | Youfeng Sun | Sewage Treatment Process and System |
| CN101638909A (en) * | 2009-08-13 | 2010-02-03 | 宁波市江北怡宁环保科技有限公司 | Green ecotypical toilet |
| WO2018066443A1 (en) * | 2016-10-03 | 2018-04-12 | 誠一 金 | Dirty wastewater purification system |
| CN106587538A (en) * | 2017-01-10 | 2017-04-26 | 上海应用技术大学 | Method for treating excrement and urine wastes |
| CN207412108U (en) * | 2017-05-16 | 2018-05-29 | 西安建筑科技大学 | A stool and urine separation toilet |
| CN108609814A (en) * | 2018-07-03 | 2018-10-02 | 夏海宗 | Toilet fecaluria recycling treatment equipment |
| CN109319897A (en) * | 2018-11-07 | 2019-02-12 | 中石化石油工程技术服务有限公司 | Co-direction stratified clarification and dehardening device for anti-fouling of heat exchange tube wall of evaporative desalination equipment |
| CN110241901A (en) * | 2019-06-25 | 2019-09-17 | 周鼎力 | A kind of environment-friendly type lavatory vehicle |
| CN112939649A (en) * | 2021-02-01 | 2021-06-11 | 北京建筑大学 | Integrated integrated wet garbage in-situ recycling treatment system and treatment method |
| CN113480009A (en) * | 2021-08-23 | 2021-10-08 | 浙江开创环保科技股份有限公司 | Membrane aeration sewage treatment system |
Non-Patent Citations (3)
| Title |
|---|
| 赵万余: "《畜禽粪污资源化利用实用技术》", 31 May 2019 * |
| 邓良平: "《农村水环境生态治理模式研究》", 31 July 2017 * |
| 郝晓地: "源分离生态效应及其资源化技术" * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115090119A (en) * | 2022-06-14 | 2022-09-23 | 北京建筑大学 | Urine-excrement-flushing water in-situ separation treatment system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114409193B (en) | 2023-05-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102775025B (en) | Municipal life wastewater treatment system with high efficiency and low energy consumption | |
| CN106430847B (en) | Intensive pig raising wastewater treatment equipment | |
| CN103848535B (en) | Multimedium renewable biological filtering method and device | |
| CN108178438A (en) | A kind of rural domestic sewage treatment system and purification method | |
| CN107381956A (en) | A kind of small towns domestic sewage processing system and method | |
| CN115872580A (en) | Biological sludge digestion reduction system and method | |
| CN101016186A (en) | Biological treatment method and device for ecological system of sewage circulation utilization | |
| CN108640442A (en) | The cycling use of water night soil-treatment lavatory of intelligence control | |
| CN114409193B (en) | Resource type source separation modularized toilet system and method for treating feces by using same | |
| CN108609814A (en) | Toilet fecaluria recycling treatment equipment | |
| CN202945124U (en) | Urban sewage treatment system with high efficiency and low energy consumption | |
| CN113149361B (en) | Wastewater treatment device and process for garbage transfer station | |
| CN109694162A (en) | A kind of remodeling septic tank of rural toilet liquid dung and sanitary wastewater processing up to standard | |
| CN206843280U (en) | A kind of medical treatment or Domestic sewage integrated treatment unit | |
| CN108640444A (en) | The intelligence control lavatory of recyclable sewage disposal | |
| CN203700114U (en) | All-in-one sewage treatment equipment | |
| CN209468279U (en) | A kind of country sewage solar wind-energy processing equipment | |
| CN219950774U (en) | Medical sewage treatment device | |
| CN218507660U (en) | Self-cleaning circulating type environment-friendly toilet | |
| CN220223874U (en) | Micro-power sewage treatment integrated device | |
| CN217025689U (en) | Organic wastewater treatment device based on microbial technology | |
| CN206940693U (en) | A kind of mobile integrated sewage disposal device of suitable the Yellow River camp buildings | |
| CN201087153Y (en) | Surface aeration impeller liftable sewage biological purification device with ventilation pipe | |
| CN210635869U (en) | Toilet excrement treatment device | |
| CN210457873U (en) | New energy rural sewage treatment and recovery system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |