Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Farming wastewater phosphorous biochemical removal process

A technology for aquaculture sewage and biochemical phosphorus removal, which is applied in the field of aquaculture sewage biochemical phosphorus removal technology, can solve the problems of neglecting the phosphorus removal effect of anoxic stage sludge and the nitrification effect of nitrifying bacteria, and achieves low treatment cost, reduced treatment cost, Effective Phosphorus Removal

Inactive Publication Date: 2019-04-23
GUANGZHOU JIAKANG ENVIRONMENTAL PROTECTION TECH
View PDF8 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Studies have found that by shortening the sludge age of aerobic sludge and increasing the amount of sludge discharged, the biochemical phosphorus removal capacity can be improved, but this will have a great impact on the nitrification of nitrifying bacteria
The traditional phosphorus removal process mainly relies on the phosphorus removal effect of the sludge in the anaerobic stage and the sludge in the aerobic stage, while ignoring the phosphorus removal effect of the sludge in the anoxic stage

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Farming wastewater phosphorous biochemical removal process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] A biochemical phosphorus removal process for aquaculture sewage, comprising the following steps:

[0029] 1) Feed the aquaculture sewage (COD=2000mg / L, ammonia nitrogen=600mg / L) into the anoxic tank for 25h anoxic treatment;

[0030] 2) Let the effluent from the anoxic tank enter the anoxic sedimentation tank by gravity, and carry out natural precipitation for 15 hours to obtain anoxic sludge and supernatant, and part of the anoxic sludge is returned to the anoxic tank (the return flow is 100% of the water inflow of the anoxic tank %), partly excludes phosphorus (the daily efflux is 3% of the anoxic pool capacity);

[0031] 3) The supernatant in the anoxic sedimentation tank is automatically flowed into the aerobic tank, and aerobic treatment is carried out for 20 hours;

[0032] 4) Return part of the effluent from the aerobic tank to the anoxic tank (the return flow rate is 200% of the water intake in the anoxic tank), and part of it flows into the aerobic sedimentati...

Embodiment 2

[0035] A biochemical phosphorus removal process for aquaculture sewage, comprising the following steps:

[0036] 1) Feed the aquaculture sewage (COD=2000mg / L, ammonia nitrogen=600mg / L) into the anoxic tank for 30h anoxic treatment;

[0037] 2) Let the effluent from the anoxic tank flow into the anoxic sedimentation tank, and carry out natural precipitation for 15 hours to obtain anoxic sludge and supernatant, and part of the anoxic sludge is returned to the anoxic tank (the return flow is 150% of the influent water in the anoxic tank. %), partly excludes phosphorus (the daily efflux is 8% of the anoxic pool capacity);

[0038] 3) The supernatant in the anoxic sedimentation tank is automatically flowed into the aerobic tank, and aerobic treatment is carried out for 25 hours;

[0039] 4) Return part of the effluent from the aerobic tank to the anoxic tank (the return flow rate is 300% of the water intake in the anoxic tank), and part of it flows into the aerobic sedimentation t...

Embodiment 3

[0042] A biochemical phosphorus removal process for aquaculture sewage, comprising the following steps:

[0043] 1) Feed the aquaculture sewage (COD=2000mg / L, ammonia nitrogen=600mg / L) into the anoxic tank for 40h anoxic treatment;

[0044] 2) Let the effluent from the anoxic tank flow into the anoxic sedimentation tank by gravity, and carry out natural precipitation for 20 hours to obtain anoxic sludge and supernatant, and part of the anoxic sludge is returned to the anoxic tank (the return flow is 200% of the water intake of the anoxic tank. %), partly excludes phosphorus (the daily efflux is 10% of the anoxic pool capacity);

[0045] 3) The supernatant in the anoxic sedimentation tank is automatically flowed into the aerobic tank, and aerobic treatment is carried out for 30 hours;

[0046] 4) Return part of the effluent from the aerobic tank to the anoxic tank (the return flow rate is 500% of the water intake in the anoxic tank), and part of it flows into the aerobic sedim...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a farming wastewater phosphorous biochemical removal process. The farming wastewater phosphorous biochemical removal process comprises the following processes of 1) feeding farming wastewater into an anaerobic pond for anaerobic treatment; 2) enabling the effluent of the anaerobic pond to automatically flow into an anaerobic precipitation pond for natural precipitation to obtain anoxic sludge and supernatant, returning a part of the anoxic sludge to the anaerobic pond and discharging the other part of the anoxic sludge for phosphorous removal; 3) enabling the supernatant of the anaerobic precipitation pond to automatically flow into an aerobic pond for aerobic treatment; 4) returning a part of the effluent of the aerobic pond to the anaerobic pond, enabling the other part of the effluent of the aerobic pond to automatically flow into an aerobic precipitation pond for natural precipitation to obtain aerobic sludge and supernatant, returning a part of the aerobicsludge to the aerobic pond, discharging the other part of the aerobic sludge for phosphorous removal, and performing subsequent treatment on the supernatant. The farming wastewater phosphorous biochemical removal process can make full use of the phosphorous removing effects of the sludge of an anaerobic section and the sludge of an aerobic section to achieve efficient phosphorous removal, avoid affecting the denitrification effects of nitrifying bacteria and be low in processing cost.

Description

technical field [0001] The invention relates to a biochemical dephosphorization process for aquaculture sewage, which belongs to the technical field of sewage treatment. Background technique [0002] At present, most of the aquaculture sewage is treated by anaerobic, anoxic and aerobic combined biochemical processes, but due to the widespread use of phosphorus-rich feed and the low absorption and utilization of phosphorus by livestock and poultry, most of the phosphorus will be discharged with manure. To the outside of the organism, the phosphorus content in the aquaculture sewage is seriously exceeded, which in turn leads to a serious imbalance in the ratio of C, N, and P in the aquaculture sewage, which greatly increases the difficulty of phosphorus removal, and the phosphorus removal effect of the aquaculture sewage is often not ideal. [0003] The principle of biochemical phosphorus removal is as follows: in the anaerobic section, phosphorus-releasing bacteria release ph...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C02F9/14C02F103/20
CPCC02F1/52C02F3/12C02F3/28C02F3/308C02F9/00C02F2001/007C02F2103/20C02F2209/08C02F2209/14C02F2209/44
Inventor 董部根
Owner GUANGZHOU JIAKANG ENVIRONMENTAL PROTECTION TECH
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products