CN105921332B - A kind of purifying treatment method that fountain effluent cycle utilizes and system - Google Patents

A kind of purifying treatment method that fountain effluent cycle utilizes and system Download PDF

Info

Publication number
CN105921332B
CN105921332B CN201610158734.1A CN201610158734A CN105921332B CN 105921332 B CN105921332 B CN 105921332B CN 201610158734 A CN201610158734 A CN 201610158734A CN 105921332 B CN105921332 B CN 105921332B
Authority
CN
China
Prior art keywords
annular
sewage
level
fountain
water spray
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.)
Active
Application number
CN201610158734.1A
Other languages
Chinese (zh)
Other versions
CN105921332A (en
Inventor
程华荣
周文君
李朋远
韩启斌
王楚君
魏燕鸿
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.)
Guangdong Praseodymium Health Care Industry Investment Co ltd
Original Assignee
Donghua Shenzhen Garden Ltd By Share Ltd
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 Donghua Shenzhen Garden Ltd By Share Ltd filed Critical Donghua Shenzhen Garden Ltd By Share Ltd
Priority to CN201610158734.1A priority Critical patent/CN105921332B/en
Publication of CN105921332A publication Critical patent/CN105921332A/en
Application granted granted Critical
Publication of CN105921332B publication Critical patent/CN105921332B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B14/00Arrangements for collecting, re-using or eliminating excess spraying material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B15/00Details of spraying plant or spraying apparatus not otherwise provided for; Accessories
    • B05B15/40Filters located upstream of the spraying outlets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B17/00Apparatus for spraying or atomising liquids or other fluent materials, not covered by the preceding groups
    • B05B17/08Fountains
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Biological Treatment Of Waste Water (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)

Abstract

A kind of purifying treatment method that fountain effluent cycle utilizes and system, a kind of purifying treatment method that fountain effluent cycle utilizes, this method include:The sewage of fountain is purified water by first order circular filter net, second level circular filter net, third level circular filter net and sewage reaction tank;Purified water is flowed into cistern in case the sparge pipe of fountain is sprayed water;The fountain includes first layer water spray annular table, second layer water spray annular table, third layer water spray annular table and the 4th layer of water spray annular table;Implement the purifying treatment method and system that the fountain effluent cycle of the present invention utilizes, has the advantages that:Realize the feasible sewage purification and dissociation of the circulating water in the fountain of park, shorten the time of sewage disposal, reduce the cost and energy consumption of sewage disposal, reach the efficient degradation of pollutant and water body efficiently separated with pollutant, realize fountain water reuse, it is effective to save water resource, it avoids wasting.

Description

A kind of purifying treatment method that fountain effluent cycle utilizes and system
Technical field
The present invention relates to field of environment protection, at a kind of purification that fountain effluent cycle utilizes Manage method and system.
Background technology
With the development of industrialization and urbanization, water environment pollution, water scarcity getting worse, water pollution control, water Environmental protection is very urgent.China creates city or city and uses rain sewage diversion system now, but mature city or old town are most It is still the run-off system of confluence of rainwater and sewage, many combined sewages are to be directly discharged to water body.And old combined canal is changed to separate system, It is limited greatly by tale quale, many old towns build up that the age is longer, and underground utilities basic forming, surface structures are crowded, and road surface is narrow Narrow, it is larger that old combined canal changes separate system difficulty.One big feature of combined sewage be the water quality in dry season and rainy season, water variation greatly, Rainy season sewage BOD concentration is low, is unfavorable for biochemical treatment.Country proposes that 2010 China's treatment rate of domestic sewage requires to reach 40%, therefore, effective combined sewage processing method is studied, had great importance to accelerating municipal sewage treatment paces.
Invention content
The technical problem to be solved by the invention is to provide a kind of purifying treatment method that fountain effluent cycle utilizes and System is reduced dirty with the time for shortening sewage disposal in the fountain in park so as to solve the deficiencies in the prior art, is realized The cost and energy consumption of water process realize fountain water reuse, effectively save water resource, avoid wasting.
The present invention solves above-mentioned technical problem, provides the technical solution solved as follows:A kind of fountain effluent cycle utilization Purifying treatment method, this method includes:
S1, the sewage of fountain is obtained by the first order circular filter net progress sewage purification of fountain at the first order Manage sewage;
S2, first order treated sewage is obtained into the second level by the second level circular filter net progress sewage purification of fountain Treated sewage;
S3, second level treated sewage is obtained into the third level by the third level circular filter net progress sewage purification of fountain Treated sewage;
S4, third level treated sewage is purified by the sewage reaction tank progress organic matter decomposition reaction of fountain Water;
S5, purified water is flowed into cistern in case the sparge pipe of fountain is sprayed water.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the fountain is four inwardly reduced The annular fountain of layer, respectively first layer water spray annular table, second layer water spray annular table, third layer water spray annular table and the 4th layer Water spray annular table;Wherein, first order annular filter pond, the second layer are provided on the outer shroud of the first layer water spray annular table It is provided with second level annular filter pond on the outer shroud for annular table of spraying water, the is provided on the outer shroud of the third layer water spray annular table Three-level annular filtering ponds, it is described 4th layer water spray annular table outer shroud on be provided with sewage reaction tank, the middle part is provided with water storages Pond.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the ring of the first layer water spray annular table Shape radius is more than the annular radius of second layer water spray annular table, and the annular radius of the second layer water spray annular table is more than third layer The annular radius of the annular radius for annular table of spraying water, the third layer water spray annular table is more than the annular radius of sewage reaction tank, The annular radius of the sewage reaction tank is more than the annular radius of cistern.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the first order annular filter is set in pond It is equipped with first order circular filter net, the first osculum and the first mudhole, the second level annular filter is provided with second in pond Grade circular filter net, the second osculum and the second mudhole are provided with third level annular mistake in third level annular filter pond Strainer, third osculum and third mudhole are provided with the 4th osculum and the 4th mudhole in the sewage reaction tank;It is described First osculum is connected between first order annular filter pond and second level annular filter pond, and second osculum is connected to Between two level annular filtering ponds and third level annular filter pond, the third osculum is connected to third level annular filter pond and dirt Between water reaction tank, the 4th osculum is connected between sewage reaction tank and cistern, and spray is provided in the cistern Water pipe.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, sludge is additionally provided in the fountain Pond, first mudhole, the second mudhole, third mudhole and the 4th mudhole are connected with sludge-tank respectively, for converging Sludge and sundries after collection filtering or after reaction.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the first order circular filter net uses Polyurethane sponge filter sewage, the second level circular filter net use activated carbon screen cloth filter sewage, the third level annular Filter screen uses the eutrophy ingredient in microorganism formulation mixed decomposition sewage;Be provided in the sewage reaction tank aerobic bacteria, Bark and sand mixing purify sewage, wherein the mixed proportion of the aerobic bacteria, fermentation bark and sand is 3:3:4, For decomposing the organic components in sewage.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the microorganism formulation is digested using sub- Spirillum, red spirillum and Bacillus acidi lactici mixing ratio are configured to.
The present invention also provides a kind of cleaning treatment system that fountain effluent cycle utilizes, which includes fountain, institute It states fountain and includes respectively first layer water spray annular table, second layer water spray annular table, third layer water spray annular table and the 4th layer Water spray annular table;Wherein, first order annular filter pond, the second layer are provided on the outer shroud of the first layer water spray annular table It is provided with second level annular filter pond on the outer shroud for annular table of spraying water, the is provided on the outer shroud of the third layer water spray annular table Three-level annular filtering ponds, it is described 4th layer water spray annular table outer shroud on be provided with sewage reaction tank, the middle part is provided with water storages Pond.
In the cleaning treatment system that utilizes of fountain effluent cycle of the present invention, first order annular filter pond, the Two level annular filtering ponds, third level annular filter pond, sewage reaction tank and cistern are sequentially connected and connect;The first order annular mistake Filter tank is provided with first order circular filter net, second level annular filter pond is provided with second level circular filter net, third level annular Filtering ponds are provided with third level circular filter net.
In the cleaning treatment system that the fountain effluent cycle of the present invention utilizes, the first order circular filter net uses Polyurethane sponge filter sewage, the second level circular filter net use activated carbon screen cloth filter sewage, the third level annular Filter screen uses the eutrophy ingredient in microorganism formulation mixed decomposition sewage;Be provided in the sewage reaction tank aerobic bacteria, Bark and sand mixing purify sewage, wherein the mixed proportion of the aerobic bacteria, fermentation bark and sand is 3:3:4, For decomposing the organic components in sewage;The microorganism formulation is using sub- digestion spirillum, red spirillum and Bacillus acidi lactici mixing Than being configured to.
Implement the purifying treatment method and system that the fountain effluent cycle of the present invention utilizes, has the advantages that: The space-time of the feasible sewage purification of circulating water and contaminant degradation is realized in gardens to dissociate, shorten sewage disposal when Between, the cost and energy consumption of sewage disposal are reduced, the efficient degradation of pollutant and water body efficiently separated with pollutant is reached, is realized Fountain water reuse, effectively saves water resource, avoids wasting.
Description of the drawings
Present invention will be further explained below with reference to the attached drawings and examples, in attached drawing:
Fig. 1 is the flow diagram for the purifying treatment method that the fountain effluent cycle of the present invention utilizes;
Fig. 2 is the structural profile illustration for the cleaning treatment system that the fountain effluent cycle of the present invention utilizes;
100, first layer is sprayed water annular table, 200, the second layer spray water annular table, 300, third layer spray water annular table, 400, the Four layers of water spray annular table, 500, cistern, 600, sparge pipe, 700, sludge-tank, 110, first order circular filter net, 120, first Osculum, the 130, first mudhole, the 210, second level circular filter net, 220, second draining, the 230, second mudhole, 310, the Three-level annular filter screen, 320, third osculum, 330, third mudhole, 410, sewage reaction tank, the 420, the 4th osculum, 430, the 4th mudhole.
Specific implementation mode
In order to make the purpose , technical scheme and advantage of the present invention be clearer, with reference to the accompanying drawings and embodiments, right The present invention is further elaborated.It should be appreciated that described herein, specific examples are only used to explain the present invention, not For limiting the present invention.
As shown in Figure 1, the flow diagram of the purifying treatment method utilized for fountain effluent cycle of the invention;It is a kind of The purifying treatment method that fountain effluent cycle utilizes, this method include:
S1, the sewage of fountain is obtained first by the progress sewage purification of first order circular filter net 110 of fountain Grade treated sewage;
S2, it first order treated sewage is subjected to sewage purification by the second level circular filter net 210 of fountain obtains the Two stage treatment sewage;
S3, it second level treated sewage is subjected to sewage purification by the third level circular filter net 310 of fountain obtains the Tertiary treatment sewage;
S4, third level treated sewage is obtained only by the progress organic matter decomposition reaction of sewage reaction tank 410 of fountain Change water;
S5, purified water is flowed into cistern 500 in case the sparge pipe 600 of fountain is sprayed water.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the fountain is four inwardly reduced The annular fountain of layer, respectively first layer water spray annular table 100, second layer water spray annular table 200, third layer water spray annular table 300 and the 4th layer water spray annular table 400;Wherein, it is provided with first order annular on the outer shroud of the first layer water spray annular table 100 Filtering ponds are provided with second level annular filter pond, the third layer water ring on the outer shroud of second layer water spray annular table 200 It is provided with third level annular filter pond on the outer shroud of shape platform 300, dirt is provided on the outer shroud of the 4th layer of water spray annular table 400 Water reaction tank 410, the middle part is provided with cisterns 500.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the first layer water spray annular table 100 Annular radius be more than the annular radius of second layer water spray annular table 200, the annular radius of second layer water spray annular table 200 The annular radius of the annular radius for annular table 300 of spraying water more than third layer, the third layer water spray annular table 300 is anti-more than sewage The annular radius in pond 410, the annular radius of the sewage reaction tank 410 is answered to be more than the annular radius of cistern 500.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the first order annular filter is set in pond It is equipped with first order circular filter net 110, the first osculum 120 and the first mudhole 130, the second level annular filter is set in pond It is equipped with second level circular filter net 210, the second osculum 220 and the second mudhole 230, the third level annular filter is set in pond It is equipped with third level circular filter net 310, third osculum 320 and third mudhole 330, is arranged in the sewage reaction tank 410 There are the 4th osculum 420 and the 4th mudhole 430;First osculum 120 is connected to first order annular filter pond and second Between grade annular filter pond, second osculum 220 be connected to second level annular filter pond and third level annular filter pond it Between, the third osculum 320 is connected between third level annular filter pond and sewage reaction tank 410, the 4th osculum 420 are connected between sewage reaction tank 410 and cistern 500, and sparge pipe 600 is provided in the cistern 500.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, sludge is additionally provided in the fountain Pond 700, first mudhole 130, the second mudhole 230, third mudhole 330 and the 4th mudhole 430 respectively with sludge Pond 700 is connected, for collect filtering after or reaction after sludge and sundries.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the first order circular filter net 110 Using polyurethane sponge filter sewage, the second level circular filter net 210 uses activated carbon screen cloth filter sewage, the third Grade circular filter net 310 is using the eutrophy ingredient in microorganism formulation mixed decomposition sewage;It is set in the sewage reaction tank 410 It is equipped with aerobic bacteria, bark and sand mixing to purify sewage, wherein the mixing of the aerobic bacteria, ferment bark and sand Ratio is 3:3:4, for decomposing the organic components in sewage.
In the purifying treatment method that the fountain effluent cycle of the present invention utilizes, the microorganism formulation is digested using sub- Spirillum, red spirillum and Bacillus acidi lactici mixing ratio are configured to, wherein the mixing of sub- the digestion spirillum, red spirillum and Bacillus acidi lactici Ratio is 4:3:4.
As shown in Fig. 2, the structural profile illustration of the cleaning treatment system utilized for fountain effluent cycle of the invention; The present invention also provides a kind of cleaning treatment system that fountain effluent cycle utilizes, which includes fountain, the fountain Including being respectively first layer water spray annular table 100, second layer water spray annular table 200, third layer water spray annular table 300 and the 4th layer Water spray annular table 400;Wherein, it is provided with first order annular filter pond on the outer shroud of the first layer water spray annular table 100, it is described Be provided with second level annular filter pond on the outer shroud of second layer water spray annular table 200, the third layer water spray annular table 300 it is outer It is provided with third level annular filter pond on ring, sewage reaction tank is provided on the outer shroud of the 4th layer of water spray annular table 400 410, the middle part is provided with cisterns 500.
In the cleaning treatment system that utilizes of fountain effluent cycle of the present invention, first order annular filter pond, the Two level annular filtering ponds, third level annular filter pond, sewage reaction tank 410 and cistern 500 are sequentially connected and connect;The first order Annular filter pond is provided with first order circular filter net 110, second level annular filter pond is provided with second level circular filter net 210, third level annular filter pond is provided with third level circular filter net 310.
In the cleaning treatment system that the fountain effluent cycle of the present invention utilizes, the first order circular filter net 110 Using polyurethane sponge filter sewage, the second level circular filter net 210 uses activated carbon screen cloth filter sewage, the third Grade circular filter net 310 is using the eutrophy ingredient in microorganism formulation mixed decomposition sewage;It is set in the sewage reaction tank 410 It is equipped with aerobic bacteria, bark and sand mixing to purify sewage, wherein the mixing of the aerobic bacteria, ferment bark and sand Ratio is 3:3:4, for decomposing the organic components in sewage;The microorganism formulation using sub- digestion spirillum, red spirillum and Bacillus acidi lactici mixing ratio is configured to, wherein the mixed proportion of the sub- digestion spirillum, red spirillum and Bacillus acidi lactici is 4:3:4.
Compared with prior art, implement the purifying treatment method and system that the fountain effluent cycle of the present invention utilizes, tool There is following advantageous effect:It realizes the space-time of the feasible sewage purification of circulating water and contaminant degradation in gardens to dissociate, contracting The short time of sewage disposal, the cost and energy consumption of sewage disposal are reduced, reaches efficiently separating and polluting for pollutant and water body The efficient degradation of object realizes fountain water reuse, effectively saves water resource, avoid wasting.
Embodiments of the present invention above described embodiment only expresses, the description thereof is more specific and detailed, but can not Therefore it is interpreted as the limitation to the scope of the claims of the present invention.It should be pointed out that for those of ordinary skill in the art, Without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to the protection model of the present invention It encloses.Therefore, the protection domain of patent of the present invention should be determined by the appended claims.

Claims (10)

1. a kind of purifying treatment method that fountain effluent cycle utilizes, which is characterized in that this method includes:
S1, the sewage of fountain is obtained into the first order by first order circular filter net (110) the progress sewage purification of fountain Treated sewage;
S2, first order treated sewage is obtained second by second level circular filter net (210) the progress sewage purification of fountain Grade treated sewage;
S3, second level treated sewage is obtained into third by third level circular filter net (310) the progress sewage purification of fountain Grade treated sewage;
S4, third level treated sewage is purified by sewage reaction tank (410) the progress organic matter decomposition reaction of fountain Water;
S5, purified water is flowed into cistern (500) in case the sparge pipe (600) of fountain is sprayed water;
Wherein, aerobic bacteria, bark and sand mixing are provided in the sewage reaction tank (410) to purify sewage, wherein The mixed proportion of the aerobic bacteria, bark and sand is 3:3:4, for decomposing the organic components in sewage.
2. the purifying treatment method that fountain effluent cycle according to claim 1 utilizes, which is characterized in that the water spray Pond is the four layers of annular fountain inwardly reduced, respectively first layer water spray annular table (100), second layer water spray annular table (200), third layer water spray annular table (300) and the 4th layer of water spray annular table (400);Wherein, the first layer water spray annular table (100) it is provided with first order annular filter pond on outer shroud, the is provided on the outer shroud of the second layer water spray annular table (200) Two level annular filtering ponds, are provided with third level annular filter pond on the outer shroud of third layer water spray annular table (300), and described the It is provided with sewage reaction tank (410) on the outer shroud of four layers of water spray annular table (400), the middle part is provided with cistern (500).
3. the purifying treatment method that fountain effluent cycle according to claim 2 utilizes, which is characterized in that described first The annular radius of layer water spray annular table (100) is more than the annular radius of second layer water spray annular table (200), the second layer water spray The annular radius of annular table (200) is more than the annular radius of third layer water spray annular table (300), the third layer water spray annular table (300) annular radius is more than the annular radius of sewage reaction tank (410), and the annular radius of the sewage reaction tank (410) is big Annular radius in cistern (500).
4. the purifying treatment method that fountain effluent cycle according to claim 2 utilizes, which is characterized in that described first Grade annular filter is provided with first order circular filter net (110), the first osculum (120) and the first mudhole (130), institute in pond It states and is provided with second level circular filter net (210), the second osculum (220) and the second mudhole in the annular filter pond of the second level (230), third level circular filter net (310), third osculum (320) and third are provided in third level annular filter pond Mudhole (330), the sewage reaction tank (410) is interior to be provided with the 4th osculum (420) and the 4th mudhole (430);It is described First osculum (120) is connected between first order annular filter pond and second level annular filter pond, second osculum (220) it is connected between second level annular filter pond and third level annular filter pond, the third osculum (320) is connected to Between three-level annular filtering ponds and sewage reaction tank, the 4th osculum (420) be connected to sewage reaction tank and cistern it Between, it is provided with sparge pipe (600) in the cistern (500).
5. the purifying treatment method that fountain effluent cycle according to claim 4 utilizes, which is characterized in that the water spray Be additionally provided with sludge-tank (700) in pond, first mudhole (130), the second mudhole (230), third mudhole (330) and 4th mudhole (430) is connected with sludge-tank (700) respectively, for collect filtering after or reaction after sludge and sundries.
6. the purifying treatment method that fountain effluent cycle according to claim 4 utilizes, which is characterized in that described first Grade circular filter net (110) uses polyurethane sponge filter sewage, the second level circular filter net (210) to use activated carbon net Cloth filter sewage, the third level circular filter net (310) use the eutrophy ingredient in microorganism formulation mixed decomposition sewage.
7. the purifying treatment method that fountain effluent cycle according to claim 6 utilizes, which is characterized in that micro- life Object preparation is configured to using sub- digestion spirillum, red spirillum and Bacillus acidi lactici mixing ratio.
8. a kind of cleaning treatment system that fountain effluent cycle utilizes, which is characterized in that the system includes fountain, the spray Pond includes first layer water spray annular table (100), second layer water spray annular table (200), third layer water spray annular table (300) and the Four layers of water spray annular table (400);Wherein, it is provided with first order annular mistake on the outer shroud of the first layer water spray annular table (100) Filter tank is provided with second level annular filter pond, the third layer water ring on the outer shroud of second layer water spray annular table (200) It is provided with third level annular filter pond on the outer shroud of shape platform (300), is arranged on the outer shroud of the 4th layer of water spray annular table (400) There is sewage reaction tank (410), the middle part is provided with cistern (500).
9. the cleaning treatment system that fountain effluent cycle according to claim 8 utilizes, which is characterized in that described first Grade annular filter pond, second level annular filter pond, third level annular filter pond, sewage reaction tank (410) and cistern (500) according to It is secondary to be connected;First order annular filter pond is provided with first order circular filter net (110), the setting of second level annular filter pond There are second level circular filter net (210), third level annular filter pond to be provided with third level circular filter net (310).
10. the cleaning treatment system that fountain effluent cycle according to claim 8 utilizes, which is characterized in that described Level-one circular filter net (110) uses polyurethane sponge filter sewage, the second level circular filter net (210) to use activated carbon Screen cloth filter sewage, the third level circular filter net (310) use microorganism formulation mixed decomposition sewage in eutrophy at Point;It is provided with aerobic bacteria, bark and sand mixing in the sewage reaction tank (410) to purify sewage, wherein described good The mixed proportion of oxygen bacterium, bark and sand is 3:3:4, for decomposing the organic components in sewage;The microorganism formulation is adopted It is configured to Asia digestion spirillum, red spirillum and Bacillus acidi lactici mixing ratio.
CN201610158734.1A 2016-03-17 2016-03-17 A kind of purifying treatment method that fountain effluent cycle utilizes and system Active CN105921332B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610158734.1A CN105921332B (en) 2016-03-17 2016-03-17 A kind of purifying treatment method that fountain effluent cycle utilizes and system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610158734.1A CN105921332B (en) 2016-03-17 2016-03-17 A kind of purifying treatment method that fountain effluent cycle utilizes and system

Publications (2)

Publication Number Publication Date
CN105921332A CN105921332A (en) 2016-09-07
CN105921332B true CN105921332B (en) 2018-08-21

Family

ID=56840283

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610158734.1A Active CN105921332B (en) 2016-03-17 2016-03-17 A kind of purifying treatment method that fountain effluent cycle utilizes and system

Country Status (1)

Country Link
CN (1) CN105921332B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110282832B (en) * 2019-07-22 2024-03-15 北京良乡蓝鑫水利工程设计有限公司 Ecological reservoir system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1453074A (en) * 2003-06-05 2003-11-05 宁波德安城市生态技术集团有限公司 Artificial fountain and its water purifying method
KR100700631B1 (en) * 2004-09-18 2007-03-28 레인보우스케이프주식회사 Pump Strainer and fountain system using the same
KR100607381B1 (en) * 2006-03-10 2006-08-03 주식회사 성호엔지니어링 Assembly type landscape fountain
CN202460928U (en) * 2012-01-19 2012-10-03 上海海洋大学 Fountain device with sewage purification and ornamental functions
CN103599869A (en) * 2013-11-29 2014-02-26 天津宏筑建筑设计有限公司 Water spraying device

Also Published As

Publication number Publication date
CN105921332A (en) 2016-09-07

Similar Documents

Publication Publication Date Title
CN104973731A (en) Domestic wastewater treatment method
CN208532535U (en) A kind of garbage percolation liquid treating system
CN108178438A (en) A kind of rural domestic sewage treatment system and purification method
CN205873999U (en) Prevent aeration systems of long -pending mud of MBR membrane group ware
CN204661385U (en) Multimedium recyclable organism filter bed
CN102285713A (en) Membrane bioreactor and water treatment control method thereof
CN105921332B (en) A kind of purifying treatment method that fountain effluent cycle utilizes and system
CN205586647U (en) Purification treatment and monitoring system that sewage cycle utilized based on ZIGBEE network
CN113149361A (en) Garbage transfer station sewage treatment device and process
CN205347148U (en) Quick reuse of reclaimed water treatment facility
CN204958681U (en) Sewage treatment device
CN205676313U (en) The cleaning treatment system that a kind of fountain effluent cycle utilizes
CN201648104U (en) Sleeve filtering device for sewage recycling
CN107188363A (en) A kind of purifying treatment method for utilizing trade effluent to be used for Urban Ecology Landscape water
CN101090868A (en) Magneting photocatalytic compact wastewater reclamation and reuse device
CN215627416U (en) Garbage transfer station sewage treatment device
CN202016932U (en) Biological strengthened amphibious plant filter system capable of treating rural domestic sewage
CN205874149U (en) Sewage regeneration recycling system with milipore filter, active carbon and microorganism
CN201447406U (en) Fecal sewage biological treatment device
CN204509052U (en) Novel micro-power sewage treatment unit
CN210635851U (en) Facultative MBR sewage treatment tank and equipment
CN204715790U (en) The biochemical Porta Potti of a kind of in-situ treatment
CN106810024A (en) A kind of processing unit for being exclusively used in sanitary sewage
CN106186585A (en) One way of life sewage water treatment method and system thereof
CN207738561U (en) A kind of sewage disposal system of microwave technology and membrane technology combination

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20221020

Address after: 518000 406, Building 1, No. 86, Xiangyang Road, Yanchuan Community, Yanluo Street, Bao'an District, Shenzhen, Guangdong

Patentee after: Guangdong Praseodymium Health Care Industry Investment Co.,Ltd.

Address before: 518000 1st floor, building 1, No. 58, Jinger Road, Huangbei street, Luohu District, Shenzhen City, Guangdong Province

Patentee before: SHENZHEN DONGHUA LANDSCAPING CO.,LTD.