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Synchronous biochemical advanced oxidation liquid waste treatment method and device

An advanced oxidation and waste liquid technology, which is applied in the field of sewage treatment, can solve the problems of hard-to-cultivate bacteria, high operating costs, and large investment, and achieve reduced initial investment and operating costs, low investment and operating costs, and easy operation and maintenance. easy effect

Active Publication Date: 2016-02-17
东莞市环境科学研究所 +1
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  • Abstract
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  • Claims
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Problems solved by technology

[0003] (1) Conventional advanced oxidation technology has a large investment and high operating cost, especially in the treatment process of high-salt, high-concentration refractory organic wastewater, but it is also difficult to treat up-to-standard discharge, and subsequent biochemical (or other technical) facilities are required , although the use of physical field coordination (such as ultrasonic, ultraviolet, microwave) can speed up the reaction speed and improve the removal rate, it is still difficult to ensure the discharge standard, and the distance between the left and right of the physical field is generally short, and the effect on the reaction device with a large diameter is poor;
[0004] (2) Biochemical treatment of high-salt, high-concentration refractory organic wastewater, regardless of anaerobic, facultative or aerobic treatment technologies, often has problems such as difficulty in cultivating bacteria or poor impact resistance, although the operating cost is lower than that of advanced oxidation technologies , but the one-time investment cost is high and the land occupation is large, and it is often difficult to meet the standards for waste liquid with complex mixed pollutants
In addition, refractory organic matter in water is difficult to decompose or utilize, and does not contribute to denitrification or even has side effects
Wastewater often lacks trace elements such as Mg, Zn, Mo, Co, Mn and Fe required for microbial metabolism, which is also an important reason for poor biochemical effects;
[0005] (3) At present, advanced oxidation and then biochemical treatment are mostly used to pre-decompose some organic matter or convert it into small molecular organic matter that can be easily decomposed by microorganisms. However, the combined investment, land occupation and operating costs of this process are high, and Advanced oxidation uses strong oxidants to have adverse effects on subsequent biochemistry (especially anaerobic);
[0006] Conventional single technology has been difficult to discharge high-salt, high-concentration refractory organic wastewater to meet increasingly stringent environmental protection requirements. Under the new situation, it is necessary to consider the combination of different technologies, or even integrate them into the same reaction device to give full play to their respective advantages. , to overcome their respective shortcomings, to ensure discharge standards

Method used

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  • Synchronous biochemical advanced oxidation liquid waste treatment method and device
  • Synchronous biochemical advanced oxidation liquid waste treatment method and device

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Experimental program
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Effect test

Embodiment 1

[0041] Such as figure 1 with figure 2 As shown, the synchronous biochemical advanced oxidation treatment waste liquid device of the present invention comprises a biological reaction tower and a dissolved air pump 1, and the dissolved air pump 1 communicates with the water suction pipe at the top of the biological reaction tower and the perforated water pipe at the bottom of the biological reaction tower, and the dissolved air pump 1 is used to The waste water is pumped from the sump into the bioreaction tower or the water in the tower is driven to circulate. The bioreaction tower has two layers of packing inside. filler such as figure 1 The carbon fiber filler 8 in the middle; the granular catalytic biological filler is placed in the middle of the biological reaction tower, the bottom of the suspended filler is 20cm away from the bottom of the biological reaction tower, the perforated water pipe is arranged at the bottom of the tower, the ultrasonic transducer horn is placed...

Embodiment 2

[0053] The difference between this embodiment and Embodiment 1 is that the material of the granular catalytic biofiller layer in this embodiment is a natural mineral material loaded with transition metal oxides. The transition metal oxide is manganese metal oxide, and the natural mineral material is attapulgite. The suspended biological filler includes strip-shaped far-infrared biological filler and high softness filler.

[0054] The upper layer is granular catalytic biological packing accounting for 3% of the volume of the bioreaction tower, and the lower layer is hanging packing accounting for 35% of the volume of the biological reaction tower; the distance between the bottom of the hanging packing and the bottom of the bioreactor tower is 40cm; the ultrasonic power of the horn of the ultrasonic transducer is 0.3 KW, the frequency is 20KHz.

[0055] The biological reaction tower adopts sequential batch processing, and alternate aeration and static processes are set during e...

Embodiment 3

[0058] The difference between this embodiment and Embodiment 1 is that: the suspended biological filler in this embodiment includes strip-shaped far-infrared biological filler and soft filler. The transition metal oxide is cobalt metal oxide, and the natural mineral material is expanded vermiculite.

[0059] The upper layer is granular catalytic biological packing accounting for 5% of the volume of the bioreaction tower, and the lower layer is hanging packing accounting for 40% of the volume of the biological reaction tower; the distance between the bottom of the hanging packing and the bottom of the bioreaction tower is 50cm; the ultrasonic power of the horn of the ultrasonic transducer is 0.5 KW, the frequency is 40KHz.

[0060] The biological reaction tower adopts sequential batch processing, and alternate aeration and static processes are set during each batch of processing. The treatment cycle is 1.5 days, and the ratio of aeration and static time during this period is 3:...

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Abstract

The invention discloses a synchronous biochemical advanced oxidation liquid waste treatment method and device. The device comprises a biological reaction tower and a gas dissolution pump. The gas dissolution pump is communicated with a water suction pipe on the top of the biological reaction tower and a through hole water pipe at the bottom of the biological reaction tower. The gas dissolution pump is used for pumping liquid waste from a water collection pool into the biological reaction tower to drive water circulation inside the tower. Two packing layers are arranged inside the biological reaction tower, wherein granular catalysis biological packing is placed on the upper layer, and suspension packing is placed on the lower layer. The granular catalysis biological packing is placed in the middle of the biological reaction tower, the water through water pipe is arranged at the bottom of the tower, and an ultrasonic transducer amplitude-change pole is placed above the biological reaction tower; the processing capacity is high, organic loads are high, the processing effect is 2-3 times higher than that of processing technologies of the same kind, the device has the advantages of being low in investment, small in occupied land and the like, the advanced oxidation technology, the ultrasonic decomposition technology and microbiological degradation technology are integrated, and the device has the advantages of being easy and convenient to operate and maintain, high in purification efficiency, low in investment and operation cost and the like, and is particularly applicable to processing organic liquid waste hard to degrade on the condition of intensified land occupation.

Description

technical field [0001] The invention belongs to the technical field of sewage treatment and relates to the treatment technology of high-salt and high-concentration refractory organic wastewater, in particular to a method and device for synchronous biochemical advanced oxidation treatment of waste liquid. Background technique [0002] At present, there are many treatment technologies for high-salt, high-concentration and refractory organic wastewater. Commonly used methods include advanced oxidation methods, physicochemical methods, and biological methods, among which advanced oxidation methods generally include Fenton, wet catalytic oxidation, and physical field collaborative advanced oxidation. Technology, biochemical methods generally include anaerobic, facultative and aerobic treatment technologies. The above several technologies have their own advantages and are suitable for the treatment of organic wastewater in different occasions. Better results can be achieved through...

Claims

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Application Information

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IPC IPC(8): C02F3/30
Inventor 邓杰帆王书杰王武树郑启勇
Owner 东莞市环境科学研究所
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