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Sewage treatment system and sewage treatment method

A sewage treatment system and sewage technology, applied in biological water/sewage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. The problem of limited rate is to achieve the effect of enriching the flora, improving the decontamination ability, and improving the quality of the effluent.

Pending Publication Date: 2021-11-05
ZHEJIANG UNIVERSITY OF SCIENCE AND TECHNOLOGY +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, during the use of ceramsite inorganic fillers, there are disadvantages such as limited microbial adhesion and film-hanging rate, which reduces the water effluent effect of the biological aerated filter.

Method used

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  • Sewage treatment system and sewage treatment method
  • Sewage treatment system and sewage treatment method
  • Sewage treatment system and sewage treatment method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] The preparation of embodiment 1 micron magnetic separation fly ash

[0047]The fly ash is screened with a magnetic separator to screen out the high-iron fly ash, and then the high-iron fly ash is ball milled, sieved and re-magnetically separated to obtain a particle size ≤ 10 μm and an iron grade between 30-50%. Medium-magnetic high-iron fly ash: place medium-magnetic high-iron fly ash in 0.1mol / L dilute hydrochloric acid for 4 minutes, put it in an oven and dry it at 110°C for 24 hours to obtain micron-sized magnetically separated fly ash.

[0048] The electron microscope picture (9000 times) of the prepared micron-scale magnetic separation fly ash is as follows figure 1 shown. figure 1 The data show that the prepared micron-scale magnetic separation fly ash is oval, with a diameter of 80-100um and a specific surface area of ​​9.7m 2 / g, the iron element content reaches 53.2%, and the main valence form is Fe 3 o 4 .

Embodiment 2

[0049] The preparation of embodiment 2 magnetic sludge charcoal

[0050] Step 1, centrifuge the Fenton sludge at 4000r / min for 8 minutes to remove excess water, then freeze-dry the centrifuged sludge at 8°C to obtain the sludge carbon precursor;

[0051] Step 2, put the sludge carbon precursor in the tube furnace, with N 2 As a protective gas, heat to 600°C, keep the temperature constant for 3 hours, and obtain magnetic sludge charcoal after cooling.

[0052] The electron micrograph (4000 times) of the prepared magnetic sludge charcoal is as follows figure 2 shown. Depend on figure 2 It can be seen that the surface of the magnetic sludge carbon is rough, with multi-level pores evenly distributed, iron oxides embedded in the carbon material, the iron content reaches 15.2%, the structure is stable, and the specific surface area reaches 109.7m 2 / g, which is conducive to the high adsorption and concentration of microorganisms and pollutants.

Embodiment 3

[0053] Embodiment 3 sewage treatment system

[0054] sewage treatment systems such as image 3 As shown, it specifically includes: water inlet pump 1, anaerobic reaction zone 2, three-phase separator 3, microporous aeration head 4, micro-oxygen reaction zone 5, water outlet pump 6, backwashing device 7, and backwashing outlet 8; Wherein, the anaerobic reaction zone 2 is an anaerobic reaction processor (UASB), and the microaerobic reaction zone 5 is an aerated biofilter, and the aerated biological filter is provided with 6 aeration heads; the anaerobic reaction zone filler is an embodiment The micron-scale magnetic separation fly ash prepared in 1, the micro-aerobic reaction zone filler is the magnetic sludge charcoal prepared in Example 2.

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Abstract

The invention discloses a sewage treatment system and a sewage treatment method, and belongs to the technical field of sewage treatment. The sewage treatment system comprises an anaerobic reaction zone and a micro-aerobic reaction zone; the micro-aerobic reaction zone is arranged at the upper part of the anaerobic reaction zone; a three-phase separator is arranged between the anaerobic reaction zone and the micro-aerobic reaction zone; a backwashing device is arranged at the upper part of the micro-aerobic reaction area; a microporous aeration head is arranged at the bottom of the micro-aerobic reaction area; the filler of the anaerobic reaction zone is magnetic separation fly ash; and the filler of the micro-aerobic reaction zone is magnetic sludge carbon. The anaerobic reaction area is an anaerobic biological treatment reactor, and the micro-aerobic reaction area is a biological aerated filter. Methane generated in the anaerobic bioreactor enters the biological aerated filter, a plug flow type stirring effect is achieved, the concentration of dissolved oxygen in the biological aerated filter can be further adjusted, the filter is made to be in a micro-aerobic condition, meanwhile, different strengthening materials are added into the anaerobic bioreactor and the biological aerated filter respectively, and the effluent quality is improved.

Description

technical field [0001] The invention relates to the technical field of sewage treatment, in particular to a sewage treatment system and a sewage treatment method. Background technique [0002] Anaerobic process is a process of biochemically degrading organic matter through the metabolism of anaerobic and facultative bacteria under anaerobic conditions to form the nutritional and environmental conditions required for anaerobic microorganisms. Anaerobic biological treatment reactor (UASB) is a device that uses anaerobic microorganisms to convert organic matter in wastewater into biogas under anaerobic conditions. Anaerobic biological treatment reactor has the advantages of low energy consumption and high efficiency. It is used in wastewater treatment in various industries Has a wide range of applications. However, in the process of anaerobic biological treatment, the methanogenic metabolism is slow and tends to become the rate-limiting stage, which easily leads to the imbalan...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/30C02F3/00C02F101/34
CPCC02F3/30C02F3/00C02F2101/345C02F2003/003
Inventor 庄海峰闵海栋梁如婷周勇涛赵宇飞詹萧颖
Owner ZHEJIANG UNIVERSITY OF SCIENCE AND TECHNOLOGY