CN107935189A - A kind of technique using algae microballoon processing sanitary sewage - Google Patents

A kind of technique using algae microballoon processing sanitary sewage Download PDF

Info

Publication number
CN107935189A
CN107935189A CN201711334764.4A CN201711334764A CN107935189A CN 107935189 A CN107935189 A CN 107935189A CN 201711334764 A CN201711334764 A CN 201711334764A CN 107935189 A CN107935189 A CN 107935189A
Authority
CN
China
Prior art keywords
algae
liquid
concentrate
microballoon
technique
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
Application number
CN201711334764.4A
Other languages
Chinese (zh)
Other versions
CN107935189B (en
Inventor
陈英
孙永跃
泮红娟
陈国华
郑华根
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.)
HANGZHOU FUYANG JIACHANG MACHINERY Co.,Ltd.
Original Assignee
陈英
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 陈英 filed Critical 陈英
Priority to CN201711334764.4A priority Critical patent/CN107935189B/en
Publication of CN107935189A publication Critical patent/CN107935189A/en
Application granted granted Critical
Publication of CN107935189B publication Critical patent/CN107935189B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • C02F3/322Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae use of algae

Abstract

The invention belongs to environmental technology field, discloses a kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:Sanitary sewage passes sequentially through grid and slurry separator, remove solid matter, it is aerated subsequently into aeration tank, it is aerated the laggard sedimentation basins of 36 48h, sedimentation time is 12 24h, and supernatant liquid enters acid-base accommodation pond, and the pH for adjusting liquid is 7 7.5, biological reaction pool is entered back into, by algae microballoon according to 100 200g:The ratio of 1 ton of liquid is inoculated in liquid, and processing time is 68 days, finally carries out algae water separation, discharges liquid.Present invention process is easy to operate, it can be achieved that the purpose of environment-friendly and green reparation, economical and efficient is environmental-friendly, of low cost, has wide range of applications.

Description

A kind of technique using algae microballoon processing sanitary sewage
Technical field
The invention belongs to environmental technology field, and in particular to a kind of technique using algae microballoon processing sanitary sewage.
Background technology
Sanitary sewage contains substantial amounts of organic matter etc., it is total the characteristics of be nitrogenous, sulfur-bearing and phosphorous height, have to water resource larger Harm, and pollute environment.Handling this method containing nitrogen sulphur phosphorus sewage at present has many kinds, mainly there is physical treatment Method, method of chemical treatment and biological treatment.Physical treatment process is simplest water treating method, it is acted on by physical separation and recycled Undissolved suspended contaminant in sewage, physical treatment process can only handle some simple sewage disposals, but handle very endless Entirely, it is difficult to reach discharge standard;Method of chemical treatment causes medicine to consume, and very big, sludge quantity is very big;Biological treatment is by biological generation Thanking dissolves the pollutant in sewage.
In recent years, as the development of biotechnology, biological treatment are repaired sewage and be increasingly valued by people.Biology Facture possesses nontoxic, and non-corrosiveness, environment friendly is strong, easy to use, need not add equipment or engineering substantially, saves money Gold input, is accept by enterprises for extensively.At present, mostly the comparison of research it is processing of the microbial inoculum to sewage, also there are some to algae The research of class treated sewage, for example, Chinese patent technology 201710430009, discloses a kind of work for purifying domestic sewage Property phycomycete community, it come treated sewage, achieves certain effect by the synergy of algae and mushroom.Sent out based on environmental protection The requirement of exhibition carrys out treated sewage, it is necessary to develop different types of biological agent.Applicant is right according to algal culture experience for many years Algae preparation is studied.
Containing nitrogen, phosphorus and other nutriments needed for a large amount of algal growns in sanitary sewage, by sewage disposal and algae Pilot scale culture combine, sewage is reached inexpensive discharge, but also the cost of microdisk electrode can be saved, at the same time Also contain many high added value products in microalgae biomass.The current report for having had some on algae treated sewage, " Wei Cheng Gen, suspended alga handle the experimental study of micro-polluted water, 2008 " to have studied suspended alga artificial to Urban River Water, city Pollutant removal character in water body in lake and secondary municipal wastewater treatment plant water outlet;" silver-colored beautiful face etc., immobilized algae denitrogenation remove Phosphorus effect disquisition, 2009 " it have studied removal effect of the algal immobilization to nitrogen phosphorus in manually preparation sewage.Handled using microalgae Sewage has good development prospect and advantage.But the factor such as the ammonia nitrogen of sewage middle and high concentration and relatively low transparency is unfavorable for The growth of microalgae, is often difficult to reach ideal effect using single microalgae treated sewage;It would therefore be desirable to develop efficient algae Class preparation is used for handling sanitary sewage.
The content of the invention
The object of the present invention is to provide a kind of technique using algae microballoon processing sanitary sewage, the technique simple possible, environment friend Good property is strong, high treating effect, of low cost, and application prospect is good.
The present invention is achieved by the following technical solution:
A kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:
Sanitary sewage passes sequentially through grid and slurry separator, removes solid matter, is aerated subsequently into aeration tank, is aerated 36- The laggard sedimentation basins of 48h, sedimentation time 12-24h, supernatant liquid enter acid-base accommodation pond, and the pH for adjusting liquid is 7-7.5, then Into biological reaction pool, algae microballoon is according to 100-200g:The ratio of 1 ton of liquid is inoculated in liquid, and processing time is 6-8 days, Algae water separation is finally carried out, discharges liquid.
Specifically,
The algae microballoon is prepared according to following technique:
By small Closterium concentrate, scenedesmus obliquus concentrate and crescent algae fibre concentrate according to 2-3:1-2:The volume of 1-2 Than being mixed to get mixing algae solution, then add account for mixing algae solution half volume concentration be 4wt% sodium alginate it is water-soluble Liquid, the urea for accounting for mixing 2% parts by weight of algae solution and the sodium acid carbonate for accounting for mixing 4% parts by weight of algae solution, stir evenly, then be added dropwise and account for The concentration for mixing 2 times of volumes of algae solution is the calcium chloride water of 2wt%, is shaken when being added dropwise, and after being added dropwise, stands 9h, is made The algae microballoon of a diameter of 3mm.
Preferably,
The preparation method of the small Closterium concentrate includes the following steps:Take the logarithm the small Closterium in growth period, 7000rpm from Heart 15min, removes supernatant, then adds sterile water, the density for adjusting frustule is 3-4 × 107Cell/mL, obtains small new Month algae concentrate.
Preferably,
The preparation method of the scenedesmus obliquus includes the following steps:Take the logarithm the scenedesmus obliquus in growth period, 5000rpm centrifugations 15min, removes supernatant, then adds sterile water, the density for adjusting frustule is 2-3 × 107Cell/mL, obtains tiltedly giving birth to grid Algae concentrate.
Preferably,
The preparation method of the crescent algae fibre includes the following steps:Take the logarithm the crescent algae fibre in growth period, 5000rpm centrifugations 10min, removes supernatant, then adds sterile water, the density for adjusting frustule is 0.5-1 × 107Cell/mL, obtains crescent Algae fibre concentrate.
Preferably,
The parameter of the biological reaction pool is:Temperature is 25-28 DEG C, Light To Dark Ratio 12:12, intensity of illumination 5000- 10000LX。
Algae of the present invention can be obtained by conventional cultural method needed for concentration algae solution, this and non-invention Innovative point, as space is limited, do not repeat one by one.
The beneficial effect that the present invention obtains mainly includes but is not limited to several aspects:
The technological operation of present invention processing sanitary sewage is easy, it can be achieved that the purpose of environment-friendly and green reparation, economical and efficient, environment friend It is good, it is of low cost, have wide range of applications;
During the present invention prepares algae microballoon, three kinds of algae are used, compatibility is reasonable, possesses preferable synergistic effect so that dirty The removal ability of COD, NH3-N, SS and TP are effectively lifted in water;
After fixation, growth and physiological property change algae of the present invention, improve the absorption to materials such as nitrogen, sulphur and phosphorus And bioaccumulation efficiency;
Algae microballoon of the present invention is used in combination using a variety of pore-foaming agents, and the pore mechanism of different pore-foaming agents is different, compared to single The effect of pore-foaming agent, obtained pore structure size reasonable, is evenly distributed, and can ensure the quantity of pore structure;
Frustule is positioned at the area of space of restriction using immobilization technology by the present invention, makes the algae of immobilization can keep itself Metabolic activity, and can recycle and recycle after successive reaction.
Figure of description
Fig. 1:Influence of the processing time to wastewater treatment efficiency.
Embodiment
Those skilled in the art can use for reference present disclosure, be suitably modified technological parameter realization.In particular, All similar substitutions and modifications are apparent to those skilled in the art, they are considered as being included in this hair It is bright.The product and method of the present invention is described by preferred embodiment, and related personnel can substantially not depart from this hair Product as described herein and method are modified or suitably changed with combining in bright content, spirit and scope, to realize and answer Use the technology of the present invention.For a further understanding of the present invention, with reference to embodiment, the present invention is described in detail.
Embodiment 1
A kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:
Sanitary sewage passes sequentially through grid and slurry separator, removes solid matter, is aerated subsequently into aeration tank, after aeration 36 Into sedimentation basin, sedimentation time 24h, supernatant liquid enters acid-base accommodation pond, and the pH for adjusting liquid is 7, enters back into biological respinse Pond, algae microballoon is according to 100g:The ratio of 1 ton of liquid is inoculated in liquid, controlled at 25 DEG C, Light To Dark Ratio 12:12, illumination Intensity is 5000LX, and processing time is 8 days, finally carries out algae water separation, discharges liquid.
The algae microballoon is prepared according to following technique:
1)Take the logarithm the small Closterium in growth period, 7000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 4 × 107Cell/mL, obtains small Closterium concentrate;
2)Take the logarithm the scenedesmus obliquus in growth period, 5000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 3 × 107Cell/mL, obtains scenedesmus obliquus concentrate;
3)Take the logarithm the crescent algae fibre in growth period, 5000rpm centrifugation 10min, remove supernatant, then add sterile water, adjust The density for saving frustule is 1 × 107Cell/mL, obtains crescent algae fibre concentrate;
4)By small Closterium concentrate, scenedesmus obliquus concentrate and crescent algae fibre concentrate according to 3:2:2 volume ratio is mixed Conjunction obtain mixing algae solution, then add account for mixing algae solution half volume concentration be 4wt% sodium alginate aqueous solution, account for Mix the urea of 2% parts by weight of algae solution and account for the sodium acid carbonate of mixing 4% parts by weight of algae solution, stir evenly, then be added dropwise and account for mixing The concentration of 2 times of volumes of algae solution is the calcium chloride water of 2wt%, is shaken when being added dropwise, and after being added dropwise, stands 8h, diameter is made For the algae microballoon of 3mm.
Embodiment 2
A kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:
Sanitary sewage passes sequentially through grid and slurry separator, removes solid matter, is aerated subsequently into aeration tank, is aerated 48h Laggard sedimentation basin, sedimentation time 12h, supernatant liquid enter acid-base accommodation pond, and the pH for adjusting liquid is 7.5, enters back into biology Reaction tank, algae microballoon is according to 200g:The ratio of 1 ton of liquid is inoculated in liquid, controlled at 28 DEG C, Light To Dark Ratio 12:12, Intensity of illumination is 10000LX, and processing time is 6 days, finally carries out algae water separation, discharges liquid.
The algae microballoon is prepared according to following technique:
1)Take the logarithm the small Closterium in growth period, 7000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 3 × 107Cell/mL, obtains small Closterium concentrate;
2)Take the logarithm the scenedesmus obliquus in growth period, 5000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 2 × 107Cell/mL, obtains scenedesmus obliquus concentrate;
3)Take the logarithm the crescent algae fibre in growth period, 5000rpm centrifugation 10min, remove supernatant, then add sterile water, adjust The density for saving frustule is 0.5 × 107Cell/mL, obtains crescent algae fibre concentrate;
4)By small Closterium concentrate, scenedesmus obliquus concentrate and crescent algae fibre concentrate according to 2:1:1 volume ratio is mixed Conjunction obtain mixing algae solution, then add account for mixing algae solution half volume concentration be 4wt% sodium alginate aqueous solution, account for Mix the urea of 2% parts by weight of algae solution and account for the sodium acid carbonate of mixing 4% parts by weight of algae solution, stir evenly, then be added dropwise and account for mixing The concentration of 2 times of volumes of algae solution is the calcium chloride water of 2wt%, is shaken when being added dropwise, and after being added dropwise, stands 9h, diameter is made For the algae microballoon of 3mm.
Embodiment 3
A kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:
Sanitary sewage passes sequentially through grid and slurry separator, removes solid matter, is aerated subsequently into aeration tank, is aerated 40h Laggard sedimentation basin, sedimentation time 16h, supernatant liquid enter acid-base accommodation pond, and the pH for adjusting liquid is 7-7.5, enters back into life Thing reaction tank, algae microballoon is according to 150g:The ratio of 1 ton of liquid is inoculated in liquid, controlled at 26 DEG C, Light To Dark Ratio 12: 12, intensity of illumination 6000LX, processing time are 7 days, finally carry out algae water separation, discharge liquid.
The algae microballoon is prepared according to following technique:
1)Take the logarithm the small Closterium in growth period, 7000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 3 × 107Cell/mL, obtains small Closterium concentrate;
2)Take the logarithm the scenedesmus obliquus in growth period, 5000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust The density of frustule is 3 × 107Cell/mL, obtains scenedesmus obliquus concentrate;
3)Take the logarithm the crescent algae fibre in growth period, 5000rpm centrifugation 10min, remove supernatant, then add sterile water, adjust The density for saving frustule is 1 × 107Cell/mL, obtains crescent algae fibre concentrate;
4)By small Closterium concentrate, scenedesmus obliquus concentrate and crescent algae fibre concentrate according to 2:2:1 volume ratio is mixed Conjunction obtain mixing algae solution, then add account for mixing algae solution half volume concentration be 4wt% sodium alginate aqueous solution, account for Mix the urea of 2% parts by weight of algae solution and account for the sodium acid carbonate of mixing 4% parts by weight of algae solution, stir evenly, then be added dropwise and account for mixing The concentration of 2 times of volumes of algae solution is the calcium chloride water of 2wt%, is shaken when being added dropwise, and after being added dropwise, stands 9h, diameter is made For the algae microballoon of 3mm.
Embodiment 4
Treated sewage compliance test result of the present invention:
By taking embodiment 1 as an example, into biological reaction pool before every major pollutants index of sewage be:COD 1186mg/ L、BOD 978 mg/L、NH3-N 209mg/L、SS 93mg/L、TP 87mg/L;
And control group is set, wherein, control group 1:Small Closterium is not added, remaining is the same as embodiment 1;Control group 2:Do not add tiltedly Raw scenedesmus, remaining is the same as embodiment 1;Control group 3:Crescent algae fibre is not added, remaining is the same as embodiment 1.After being managed by each group other places, Testing result is shown in Table 1:
Table 1
Group Embodiment 1(mg/L) Control group 1(mg/L) Control group 2(mg/L) Control group 3(mg/L)
COD 28.1 108.6 153.7 82.0
BOD 19.4 87.1 112.9 68.5
NH3-N 13.6 31.4 59.7 28.8
SS 10.3 26.8 34.5 21.4
TP 7.4 18.4 30.2 22.7
Conclusion:As shown in table 1, by embodiment 1, control group 1-3 processing after, COD, BOD, NH3-N, SS in sanitary sewage And the pollutant level such as TP substantially reduces, by comparing, the ability of 1 group of treated sewage of embodiment is substantially better than control group 1-3, Illustrate that three kinds of algae of 1 group of embodiment can be with symbiosis, compatibility is reasonable, possesses preferable synergistic effect.
Embodiment 5
Influence of the processing time to wastewater treatment efficiency:
By taking embodiment 1 as an example, into biological reaction pool before every major pollutants index of sewage be:COD 1186mg/ L、BOD 978 mg/L、NH3-N 209mg/L、SS 93mg/L、TP 87mg/L;Respectively at the 2nd day, the 4th day, the 6th day, the 8th My god, the 10th day, the index of each pollutant in sampling Detection sewage, as shown in Figure 1, increasing over time, respectively polluted in sewage Thing declines substantially, and after the 6th day, decrease speed starts to slow down, and by the 8th day, free of contamination decline was the most obvious, then to the 10th My god, each pollutant index has been lifted, and may be better than the concentration reduction of pollutant and enough nutrients can not be provided to algae, cause Algae Mortality, so as to cause deteriorating water quality.
Finally it should be noted that:The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations;Although reference The present invention is described in detail in previous embodiment, it will be understood by those of ordinary skill in the art that:It still can be right Technical solution described in previous embodiment is modified, or carries out equivalent substitution to which part technical characteristic;And these Modification is replaced, and the essence of appropriate technical solution is departed from the spirit and scope of technical solution of the embodiment of the present invention.

Claims (6)

1. a kind of technique using algae microballoon processing sanitary sewage, it includes the following steps:
Sanitary sewage passes sequentially through grid and slurry separator, removes solid matter, is aerated subsequently into aeration tank, is aerated 36- 48h, enters back into sedimentation basin, sedimentation time 12-24h, and supernatant liquid enters acid-base accommodation pond, and the pH for adjusting liquid is 7-7.5, Biological reaction pool is entered back into, by algae microballoon according to 100-200g:The ratio of 1 ton of liquid is inoculated in liquid, processing time 6-8 My god, algae water separation is finally carried out, discharges liquid.
2. technique according to claim 1, it is characterised in that the algae microballoon is prepared according to following technique:
By small Closterium concentrate, scenedesmus obliquus concentrate and crescent algae fibre concentrate according to 2-3:1-2:The volume of 1-2 Than being mixed to get mixing algae solution, then add account for mixing algae solution half volume concentration be 4wt% sodium alginate it is water-soluble Liquid, the urea for accounting for mixing 2% parts by weight of algae solution and the sodium acid carbonate for accounting for mixing 4% parts by weight of algae solution, stir evenly, then be added dropwise and account for The concentration for mixing 2 times of volumes of algae solution is the calcium chloride water of 2wt%, is shaken when being added dropwise, and after being added dropwise, stands 9h, is made The algae microballoon of a diameter of 3mm.
3. technique according to claim 2, it is characterised in that the preparation method of the small Closterium concentrate includes as follows Step:Take the logarithm the small Closterium in growth period, 7000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust algae The density of cell is 3-4 × 107Cell/mL, obtains small Closterium concentrate.
4. technique according to claim 2, it is characterised in that the preparation method of the scenedesmus obliquus includes the following steps: Take the logarithm the scenedesmus obliquus in growth period, 5000rpm centrifugation 15min, remove supernatant, then add sterile water, adjust frustule Density be 2-3 × 107Cell/mL, obtains scenedesmus obliquus concentrate.
5. technique according to claim 2, it is characterised in that the preparation method of the crescent algae fibre includes following step Suddenly:Take the logarithm the crescent algae fibre in growth period, 5000rpm centrifugation 10min, remove supernatant, then add sterile water, adjust algae The density of cell is 0.5-1 × 107Cell/mL, obtains crescent algae fibre concentrate.
6. technique according to claim 2, it is characterised in that the parameter of the biological reaction pool is:Temperature is 25-28 DEG C, Light To Dark Ratio 12:12, intensity of illumination 5000-10000LX.
CN201711334764.4A 2017-12-14 2017-12-14 Process for treating domestic sewage by using algae microspheres Active CN107935189B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711334764.4A CN107935189B (en) 2017-12-14 2017-12-14 Process for treating domestic sewage by using algae microspheres

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711334764.4A CN107935189B (en) 2017-12-14 2017-12-14 Process for treating domestic sewage by using algae microspheres

Publications (2)

Publication Number Publication Date
CN107935189A true CN107935189A (en) 2018-04-20
CN107935189B CN107935189B (en) 2020-12-22

Family

ID=61943158

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711334764.4A Active CN107935189B (en) 2017-12-14 2017-12-14 Process for treating domestic sewage by using algae microspheres

Country Status (1)

Country Link
CN (1) CN107935189B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107988079A (en) * 2018-01-17 2018-05-04 陈英 A kind of compound algae preparation for removing nitrogen and phosphorus pollutants
CN110272123A (en) * 2019-07-03 2019-09-24 湘潭大学 A method of immobilized algal-bacteria syntaxial system denitrogenation dephosphorizing efficiency is improved with inorganic carbon source

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103739075A (en) * 2013-12-09 2014-04-23 苏州市相城区新时代特种水产养殖场 Treatment method of aquacultural waste water
CN104630295A (en) * 2015-03-08 2015-05-20 中国海洋大学 Method for treating municipal secondary wastewater and producing grease by using immobilized microalgae
CN106916260A (en) * 2017-03-29 2017-07-04 中山大学惠州研究院 A kind of preparation method of hud typed porous high water absorption microballoon
CN107140742A (en) * 2017-06-05 2017-09-08 舟山市普陀兴海养殖优质种苗选育研究所 A kind of mixed type algae water cleanser and its application

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103739075A (en) * 2013-12-09 2014-04-23 苏州市相城区新时代特种水产养殖场 Treatment method of aquacultural waste water
CN104630295A (en) * 2015-03-08 2015-05-20 中国海洋大学 Method for treating municipal secondary wastewater and producing grease by using immobilized microalgae
CN106916260A (en) * 2017-03-29 2017-07-04 中山大学惠州研究院 A kind of preparation method of hud typed porous high water absorption microballoon
CN107140742A (en) * 2017-06-05 2017-09-08 舟山市普陀兴海养殖优质种苗选育研究所 A kind of mixed type algae water cleanser and its application

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王宝贞 等: "《水污染控制工程》", 30 April 1990, 高等教育出版社 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107988079A (en) * 2018-01-17 2018-05-04 陈英 A kind of compound algae preparation for removing nitrogen and phosphorus pollutants
CN107988079B (en) * 2018-01-17 2020-12-01 内蒙古优水环保科技有限公司 Compound algae preparation for removing nitrogen and phosphorus pollutants
CN110272123A (en) * 2019-07-03 2019-09-24 湘潭大学 A method of immobilized algal-bacteria syntaxial system denitrogenation dephosphorizing efficiency is improved with inorganic carbon source

Also Published As

Publication number Publication date
CN107935189B (en) 2020-12-22

Similar Documents

Publication Publication Date Title
Wang et al. A novel shortcut nitrogen removal process using an algal-bacterial consortium in a photo-sequencing batch reactor (PSBR)
Zhao et al. Evaluation of revolving algae biofilm reactors for nutrients and metals removal from sludge thickening supernatant in a municipal wastewater treatment facility
Abdel-Raouf et al. Microalgae and wastewater treatment
CN102336498B (en) Nitrogen-phosphorus wastewater treating method by sequencing batch reactor coupled photobioreactor
ES2736248T3 (en) Method to reduce sludge produced by wastewater treatment facilities
Leong et al. Pollution prevention and waste phycoremediation by algal-based wastewater treatment technologies: The applications of high-rate algal ponds (HRAPs) and algal turf scrubber (ATS)
Sun et al. Performance and microbial community analysis of an algal-activated sludge symbiotic system: Effect of activated sludge concentration
CN101898830B (en) Complex enzyme preparation for sewage treatment and application method thereof
CN106396112A (en) Composite system used for purifying high ammonia nitrogen pig breeding biogas slurry via algae-bacterium symbiosis/ecological floating bed combined technology
CN105859033A (en) Domestic sewage treatment process
CN107603909A (en) Sewage treatment microbial inoculant and its application method
Choi et al. Co-culture consortium of Scenedesmus dimorphus and nitrifiers enhances the removal of nitrogen and phosphorus from artificial wastewater
Ariza Photo-Activated Sludge: a novel algal-bacterial biotreatment for nitrogen removal from wastewater
Soroosh et al. Influence of hydraulic retention time on municipal wastewater treatment using microalgae-bacteria flocs in sequencing batch reactors
CN107935189A (en) A kind of technique using algae microballoon processing sanitary sewage
CN103043869A (en) Recycling sewage treatment equipment by utilizing automatic backflow reactor and sewage treatment method thereof
CN105481102B (en) A kind of remodeling method of promoting to a higher rank with microbial cleaning skill upgrading sewage effluents water quality
Soroosh et al. Influence of supplementary carbon on reducing the hydraulic retention time in microalgae-bacteria (MaB) treatment of municipal wastewater
Sreesai et al. Nutrient recycling by chlorella vulgaris from septage effluent of the Bangkok city, Thailand
KR19990030821A (en) O using microorganisms in aeration tanks; Microbial treatment agent for wastewater treatment and its manufacturing method
Huang et al. Nitrogen and phosphorus removal by coupling Anaerobic ammonia oxidation reaction with algal-bacterial symbiotic system
CN102659284A (en) Regenerated papermaking wastewater treatment system and process
Khanzada et al. Growing fresh water microalgae in high ammonium landfill leachate
CN106745815A (en) It is a kind of to improve the water treatment agent that biochemical system goes ammonia nitrogen ability
CN103342438A (en) Sewage and sludge processing 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
TA01 Transfer of patent application right

Effective date of registration: 20201207

Address after: 310000 Xin Deng Zhen Wu Li Qiao Cun, Fuyang District, Hangzhou City, Zhejiang Province

Applicant after: HANGZHOU FUYANG JIACHANG MACHINERY Co.,Ltd.

Address before: Hangzhou City, Zhejiang province 311400 Fuyang District Xu Kou Zhen Jin Cicun (Hangzhou Fuyang Hongxin Ecological Agriculture Development Co., Ltd.)

Applicant before: Chen Ying

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant