CN1239403C - Sewage and waste water treating apparatus and method with natural organic polymer flocculant - Google Patents

Sewage and waste water treating apparatus and method with natural organic polymer flocculant Download PDF

Info

Publication number
CN1239403C
CN1239403C CN 03135498 CN03135498A CN1239403C CN 1239403 C CN1239403 C CN 1239403C CN 03135498 CN03135498 CN 03135498 CN 03135498 A CN03135498 A CN 03135498A CN 1239403 C CN1239403 C CN 1239403C
Authority
CN
China
Prior art keywords
tank
sewage
water
sludge
mud
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.)
Expired - Fee Related
Application number
CN 03135498
Other languages
Chinese (zh)
Other versions
CN1486939A (en
Inventor
李显贵
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Qingyuan Environmental Protection Technology Co Ltd
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN 03135498 priority Critical patent/CN1239403C/en
Publication of CN1486939A publication Critical patent/CN1486939A/en
Application granted granted Critical
Publication of CN1239403C publication Critical patent/CN1239403C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The present invention relates to a device for treating dirty/waste water with naturalness organic polymer flocculant and a method thereof. The device which comprises a grille tank, a collection tank, a regulation tank, a reaction tank, a sedimentation tank, a filtration and disinfection chamber and a clear water pond is characterized in that a sewage pump whose water discharge pipeline is provided with a branch tube for adding naturalness organic polymer flocculant is arranged at the side of the regulation tank; the reaction tank is provided with a mixing machine; the device also comprises a sludge condensation tank and a filter press. The method has the following steps: the dirty/waste water is led into the grille tank, then enters the collection tank, and finally, enters the regulation tank for influx; the dirty/waste water in the regulation tank is sucked in the reaction tank by starting the sewage pump and treated by adding naturalness polymer flocculant, and then the treated water enters the sedimentation tank; supernatant liquid in the sedimentation tank enters the filtration and disinfection chamber, and then enters the clear water pond; the water in the clear water pond is detected by sampling, and the emission standard is achieved; additionally, the method also comprises the steps of sludge treatment. The present invention has advantages of quick reaction speed and simple technology. Besides, the treated dirty/waste water can achieve the emission standard, and the generated sewage sludge can be used as vegetal flower fertilizer.

Description

A kind of polymeric flocculant is handled the device and method of sewage/wastewater
Technical field
The present invention relates to sewage disposal technology, be specifically related to the device and method that a kind of polymeric flocculant is handled sewage/wastewater.
Background technology
The sewage or waste water that produces in production and the life is serious day by day to the pollution of environment, has progressively caused people's great attention.In the socioeconomic while of fast development, must strengthen protection to environment, become people's common recognition.For a long time, many engineering technical personnel are devoted to the processing research work of sewage or waste water, have proposed the treatment process and the equipment of multiple sewage or waste water.Biological process is arranged, physico-chemical processes is also arranged.Special-purpose treatment process is arranged, as the treatment process of the treatment process of the integrated conduct method of paper waste, leather-making waste water, dyeing waste water, municipal sewage treatment method etc., but the deficiency that exists is that investment is big, occupation of land is many, the time is long, working cost is high, the water quality inferiority after the processing; General method of wastewater treatment is also arranged, as Patent Office of the People's Republic of China on November 4th, 1998 bulletin number of patent application be 98102170, name is called " common waste water treating method ".This method is with lime or contain CaO or Ca (OH) 2Material and acid effect form throw out, in forming the throw out process and throw out adsorb after forming and carry charged impurity particle and electric neutrality impurity particle in the waste water secretly, realize various wastewater such as papermaking, printing and dyeing, food-processing, brewage, the sewage in trade effluent such as chemical industry, pharmacy, dyestuff, metallurgy and city domestic sewage and rivers, lake etc. handles.Waste water though supernatant water can reach emission standard, needs to consume a large amount of lime after this method is handled, and the big inconvenience of settled sludge quantity directly utilizes.
Summary of the invention
One of purpose of the present invention provides the device that a kind of polymeric flocculant is handled sewage/wastewater, it need equipment few, take up an area of less, working cost is low, stable, has the ability of strong anti-shock loading;
Another object of the present invention provides the method that a kind of polymeric flocculant is handled sewage/wastewater, and its technology is simple, easy and simple to handle, not influenced by temperature, and soil removability is strong, can reach emission standard after the sewage disposal, and the mud of generation can be made fertilizers for potted flowers.
A kind of polymeric flocculant of the present invention is handled the device of sewage/wastewater, comprise grating tank, the water collecting basin that communicates with grating tank, the equalizing tank that communicates with water collecting basin, the reaction tank adjacent, the settling tank that communicates with reaction tank, the filter-sterilized pond that communicates with settling tank, the clean water basin that communicate with the filter-sterilized pond with equalizing tank, the other sump pump that is provided with of equalizing tank, the water-in of sump pump stretches in the equalizing tank, water outlet is located in the reaction tank, is provided with the arm that adds polymeric flocculant on the sump pump outlet conduit; Be provided with stirrer at reaction tank.
A kind of polymeric flocculant of the present invention is handled the device of sewage/wastewater, also comprise sludge thickener, pressure filter, inlet pipe communicates with sludge thickener with the mud pump outlet that equalizing tank and settling tank bottom communicate, and inlet pipe is corresponding with pressure filter with another mud pump outlet that the sludge thickener bottom communicates.
The grating tank that is used to dispose of sewage, water collecting basin, equalizing tank, reaction tank, settling tank, filter-sterilized pond, clean water basin, sludge thickener are arranged compact, equipment such as sump pump, stirrer, sludge pump, pressure filter are installed in corresponding position, to reduce floor space.
A kind of polymeric flocculant of the present invention is handled the method for sewage/wastewater, and its step is as follows:
Sewage/wastewater is introduced grating tank, remove bigger foreign material and floating matter after, enter water collecting basin, the silt particle that proportion is bigger in the sewage is fallen at the bottom of the pond, enter equalizing tank again and compile, regulate water quality, the water yield, be that next procedure keeps the stable water quality and the water yield;
Start sump pump with in the sewage suction reaction tank in the equalizing tank, and press the polymeric flocculant that sump pump discharge capacity hourly adds 0.15-1.5 ‰, start the stirrer that is contained on the reaction tank simultaneously and stir, the add-on of flocculation agent is determined with different trade effluent water quality according to sanitary sewage.Add the radically reform polymer QH flocculation agent of environment protection treating Engineering Co., Ltd development of Chongqing, this flocculation agent is to extract macromolecular compound from plant, by grafting, draw hydroxyl, amido, carboxymethyl etc., be mixed with inorganics is compound again, add the electrostatic double layer that can compress the pollutent colloidal particle in the sewage rapidly, the formation net of building bridge is simultaneously caught, and fast pollutants in sewage is condensed into the bigger flock of density, rely on the action of gravity natural subsidence, remove pollutants in sewage.
Sewage enters settling tank after flocculation treatment, rely on action of gravity to fall Yu Chidi naturally, realizes solid-liquid separation, removes pollutent;
Enter the filter-sterilized pond through the supernatant liquor of post precipitation from the top of settling tank, the fine suspension Filtration Adsorption with residual enters clean water basin again;
From clean water basin, take a sample and detect, reach emission standard, can discharge or recycle.
Described a kind of polymeric flocculant is handled the method for sewage/wastewater, and is further comprising the steps of:
Mud is got rid of: respectively the mud of equalizing tank, settling tank bottom is evacuated to sludge thickener with sludge pump.
Mud concentrates: in sludge thickener, carries out, and from mud natural subsidence the pond that extract out equalizing tank, settling tank bottom, supernatant liquor flow automatically back equalizing tank, processing once more.
Sludge press filtration: with dewatering on the mud suction pressure filter of sludge pump with the sludge thickener bottom, the water that removes returns in the equalizing tank, handles once more.
Adopt present method to handle sewage/wastewater, speed of response is fast, technology is simple, and the treatment time is short, phosphor-removing effect is remarkable especially, can reach emission standard after the sewage disposal, and the mud of generation do not expand, nontoxic, can make the plant fertilizers for potted flowers.Be applicable to and handle various trade effluents and city domestic sewage.
Description of drawings
Fig. 1 device floor plan of the present invention synoptic diagram.
Fig. 2 is a process flow diagram of the present invention.
Embodiment
Referring to Fig. 1, existing day to handle 2000M 3Sewage (city domestic sewage or trade effluent) is example, and device of the present invention is further described below:
According to the day amount of the disposing of sewage construction volume equalizing tank suitable with it, grating tank and water collecting basin are near a side of equalizing tank, grating tank communicates with water collecting basin, water collecting basin communicates with equalizing tank, the opposite side of equalizing tank with after answer the pond adjacent, settling tank and reaction tank near and communicate, filter-sterilized pond and settling tank near and communicate, clean water basin and filter-sterilized pond near and communicate, sump pump is installed in the equalizing tank next door, the water-in of sump pump stretches in the equalizing tank, water outlet connects reaction tank, and the arm that adds polymeric flocculant is installed on the sump pump outlet conduit, at reaction tank many stirrers is installed; Sludge thickener and pressure filter are arranged near the above device, the inlet pipe of a sludge pump communicates with equalizing tank and settling tank bottom, the mud pump outlet communicates with sludge thickener, and the inlet pipe of another sludge pump communicates with the sludge thickener bottom, and its outlet is corresponding with pressure filter.
Referring to Fig. 2, still handle 2000M with day 3Sewage (city domestic sewage or trade effluent) is example, and method of the present invention is further narrated:
Sewage/wastewater is introduced grating tank, remove bigger foreign material and floating matter after, enter water collecting basin, the silt particle that proportion is bigger in the sewage is fallen at the bottom of the pond, enter equalizing tank again and compile, regulate water quality, the water yield, be that next procedure keeps the stable water quality and the water yield;
Start discharge capacity and be 85 villages/hour sump pump with in the sewage suction reaction tank in the equalizing tank, and add the radically reform polymeric flocculant of environment protection treating Engineering Co., Ltd development of 1.5 ‰ Chongqing by sump pump discharge capacity hourly, starting the stirrer that is contained on the reaction tank simultaneously stirs, compress the electrostatic double layer of pollutent colloidal particle rapidly, the formation net of building bridge is simultaneously caught, fast pollutants in sewage is condensed into the bigger flock of density, relies on the action of gravity natural subsidence.
Sewage enters settling tank after flocculation treatment, rely on action of gravity to fall Yu Chidi naturally, realizes solid-liquid separation, removes pollutent;
Enter the filter-sterilized pond through the supernatant liquor of post precipitation from the top of settling tank, the fine suspension Filtration Adsorption with residual enters clean water basin again;
From clean water basin, take a sample and detect, reach emission standard, can discharge or recycle.
Present method is further comprising the steps of:
Mud is got rid of: respectively the mud of equalizing tank, settling tank bottom is evacuated to sludge thickener with sludge pump.
Mud concentrates: in sludge thickener, carries out, and from mud natural subsidence the pond that extract out equalizing tank, settling tank bottom, supernatant liquor flow automatically back equalizing tank, processing once more.
Sludge press filtration: with dewatering on the mud suction pressure filter of sludge pump with the sludge thickener bottom, the water that removes returns in the equalizing tank, handles once more.
Adopt said apparatus and handle as stated above after the clear water that obtains under the situation that does not increase other control measures, water quality has reached the first discharge standard of relevant town B-grade sewage treatment plant requirement among the GB8978-96 " integrated wastewater discharge standard ".The working cost that present method is handled one ton of sewage is 0.35 yuan, than the working cost low about 30% of general sewage work.

Claims (4)

1, a kind of polymeric flocculant is handled the device of sewage/wastewater, comprise grating tank, the water collecting basin that communicates with grating tank, the equalizing tank that communicates with water collecting basin, it is characterized in that reaction tank and equalizing tank are adjacent, settling tank communicates with reaction tank, the filter-sterilized pond communicates with settling tank, and clean water basin communicate with the filter-sterilized pond; Be provided with sump pump on the equalizing tank side, the water-in of sump pump stretches in the equalizing tank, and water outlet is located in the reaction tank; On the sump pump outlet conduit, be provided with the arm that adds polymeric flocculant; Be provided with stirrer at reaction tank.
2, a kind of polymeric flocculant according to claim 1 is handled the device of sewage/wastewater, also comprise sludge thickener, pressure filter, it is characterized in that inlet pipe communicates with sludge thickener with the mud pump outlet that equalizing tank and settling tank bottom communicate, inlet pipe is corresponding with pressure filter with another mud pump outlet that the sludge thickener bottom communicates.
3, a kind of polymeric flocculant is handled the method for sewage/wastewater, and its step is as follows:
Sewage/wastewater is introduced grating tank, remove bigger foreign material and floating matter after, enter water collecting basin, the silt particle that proportion is bigger in the sewage is fallen at the bottom of the pond, enter equalizing tank again and compile, regulate water quality, the water yield, be that next procedure keeps the stable water quality and the water yield;
Start sump pump with in the sewage suction reaction tank in the equalizing tank, and press the polymeric flocculant that sump pump discharge capacity hourly adds 0.15-1.5 ‰, start the stirrer that is contained on the reaction tank simultaneously and stir;
Sewage enters settling tank after flocculation treatment, rely on action of gravity to fall Yu Chidi naturally, realizes solid-liquid separation, removes pollutent;
Enter the filter-sterilized pond through the supernatant liquor of post precipitation from the top of settling tank, the fine suspension Filtration Adsorption with residual enters clean water basin again;
From clean water basin, take a sample and detect, reach emission standard, can discharge or recycle.
4, a kind of polymeric flocculant according to claim 3 is handled the method for sewage/wastewater, and is further comprising the steps of:
Mud is got rid of: respectively the mud of equalizing tank, settling tank bottom is evacuated to sludge thickener with sludge pump;
Mud concentrates: in sludge thickener, carries out, and from mud natural subsidence the pond that extract out equalizing tank, settling tank bottom, supernatant liquor flow automatically back equalizing tank, processing once more;
Sludge press filtration: with dewatering on the mud suction pressure filter of sludge pump with the sludge thickener bottom, the water that removes returns in the equalizing tank, handles once more.
CN 03135498 2003-07-28 2003-07-28 Sewage and waste water treating apparatus and method with natural organic polymer flocculant Expired - Fee Related CN1239403C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 03135498 CN1239403C (en) 2003-07-28 2003-07-28 Sewage and waste water treating apparatus and method with natural organic polymer flocculant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 03135498 CN1239403C (en) 2003-07-28 2003-07-28 Sewage and waste water treating apparatus and method with natural organic polymer flocculant

Publications (2)

Publication Number Publication Date
CN1486939A CN1486939A (en) 2004-04-07
CN1239403C true CN1239403C (en) 2006-02-01

Family

ID=34154668

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 03135498 Expired - Fee Related CN1239403C (en) 2003-07-28 2003-07-28 Sewage and waste water treating apparatus and method with natural organic polymer flocculant

Country Status (1)

Country Link
CN (1) CN1239403C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109264905A (en) * 2018-10-08 2019-01-25 成都瑞索斯再生资源回收有限公司 It is a kind of for construction refuse regenerated sewage disposal system

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100393642C (en) * 2004-08-13 2008-06-11 任伟东 Sewage recorery treatment system
WO2009116463A1 (en) * 2008-03-17 2009-09-24 株式会社クボタ Purifying tank
CN102001772A (en) * 2010-12-17 2011-04-06 攀枝花钢城集团有限公司 Method for treating industrial waste sewage
CN102863102A (en) * 2012-10-18 2013-01-09 中煤科工集团武汉设计研究院 Wastewater treatment device and method of long-distance pipeline coal handling terminal
CN103420536B (en) * 2013-08-30 2016-01-20 北京英特环科水处理工程设备有限公司 A kind of leather waste water recycling treatment facility and method
JP6885826B2 (en) * 2016-09-15 2021-06-16 デクセリアルズ株式会社 Water purification agent manufacturing method and wastewater treatment method
CN108996570A (en) * 2018-08-20 2018-12-14 朱翠帮 A kind of method of treated sewage treatment discharge
CN110386691B (en) * 2019-07-24 2021-11-23 温州众新建设有限公司 Municipal administration sewage treatment plant
CN110655230A (en) * 2019-10-08 2020-01-07 赣州江钨新型合金材料有限公司 Treatment method of circulating water for copper material production
CN112062324A (en) * 2020-07-27 2020-12-11 湖北国创道路工程有限公司 Sewage overflow port strengthening pretreatment process
CN114314940A (en) * 2022-01-17 2022-04-12 上海奥栋机电有限公司 Sewage treatment device
CN114409116B (en) * 2022-01-28 2023-06-23 山东绿立冠环保科技有限公司 Full-automatic wastewater integrated multi-stage treatment equipment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109264905A (en) * 2018-10-08 2019-01-25 成都瑞索斯再生资源回收有限公司 It is a kind of for construction refuse regenerated sewage disposal system

Also Published As

Publication number Publication date
CN1486939A (en) 2004-04-07

Similar Documents

Publication Publication Date Title
CN1239403C (en) Sewage and waste water treating apparatus and method with natural organic polymer flocculant
KR101346525B1 (en) Device to cohere and to dispose of wastes water
CN207294524U (en) A kind of landfill leachate film processing system
CN1556052A (en) Treatment technology of emulsion contained spent water
CN1163425C (en) Method and apparatus for treating sewage from catering business
CN101585611B (en) Industrial wastewater and municipal wastewater treatment method
CN209081580U (en) A kind of city garbage percolate pretreatment system
CN215250222U (en) Multistage purification and magnetic separation heavy metal wastewater treatment system
CN214829727U (en) Device for preparing organic carbon source from kitchen waste water
CN213569948U (en) Sewage treatment tank
CN212610023U (en) Small-size portable modularization sewage treatment platform
CN110104897A (en) A kind of percolation liquid treating system of household refuse landfill sites
CN201268648Y (en) Multifunctional universal sewage treatment system
RU2321553C2 (en) Method of removal and decontamination of silt sediments of sewage water and technological line for realization of this method
CN101293724A (en) Miniature general use sewage treatment system
CN1162361C (en) Sludge concentration dehydration treatment device
CN1259246C (en) Scruff collecting method in processing sewage
CN211546259U (en) Integrated high ammonia nitrogen wastewater treatment device
JPH0924383A (en) Treatment of waste water of car washing and device therefor
CN212894324U (en) Be applied to multistage baffling anaerobic reaction device of pharmacy waste water
CN1168676C (en) Contaminated-fluid treating filter method and equipment
CN1450007A (en) Biological comprehensive treatment method for domestic organic refuse and sewage and used treatment system thereof
CN213625986U (en) Wastewater collection device for municipal road drainage
CN2908486Y (en) Mixed liquid sludge drying treatment equipment of small membrane biotogical reactor
Shammas et al. A compact flotation–filtration tertiary treatment unit for wastewater reuse

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
ASS Succession or assignment of patent right

Owner name: CHONGQING QINGYUAN ENVIRONMENTAL PROTECTION TECHNO

Free format text: FORMER OWNER: LI XIANGUI

Effective date: 20110914

C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20110914

Address after: Jiulongpo District of Chongqing City Heng Jie Shi Pingqiao 400050 yuan with special No. 6 No. 18-1

Patentee after: Chongqing Qingyuan Environmental Protection Technology Co., Ltd.

Address before: 400050 street is Chongqing Jiulongpo District Yangjiaping 25 Building No. 6 Chongqing Qingyuan Environmental Protection Company.

Patentee before: Li Xiangui

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20060201

Termination date: 20180728