Deep-well aerobic digestive treatment device and treating method for organic sludge

A technology for digestion and treatment of organic sludge, applied in sludge treatment, biological sludge treatment, etc., can solve the problems of increased investment and treatment costs, long hydraulic retention time, increased reactor volume, etc., to achieve reduced aeration and Effects of energy consumption, saving operating costs, and improving degradation removal rate and efficiency

Inactive Publication Date: 2012-11-28
山东汇盛天泽环境工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This method requires a longer hydraulic retention time, which not only increases the volume of the reactor, but also greatly increases the investment and treatment costs, and the current relationship between operating parameters and the growth of micro-animals, and how to control and maintain micro-animals under high-density conditions Long-term growth and other aspects of research are not enough, not suitable for large-scale promotion

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  • Deep-well aerobic digestive treatment device and treating method for organic sludge
  • Deep-well aerobic digestive treatment device and treating method for organic sludge

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Embodiment Construction

[0034] Such as figure 1 As shown, the organic sludge deep-well aerobic digestion treatment device includes a reactor body 1 and a top box 2. The reactor body 1 is provided with an aeration device 3, a mud inlet pipe 4, and an aeration inlet pipe 5, The air inlet pipe 12 for circulation, the mud outlet pipe 6, the air inlet pipe 5 for aeration, and the air inlet pipe 12 for circulation are connected to an air compressor 7.

[0035] Wherein, the mud outlet 41 of the mud inlet pipe 4 is located in the middle of the reactor body 1 in the axial direction and the mud outlet direction is upward.

[0036] The air outlet 51 of the air inlet pipe 5 for aeration is lower than the mud outlet 41 of the mud inlet pipe 4.

[0037] The mud inlet 61 of the mud outlet pipe 6 is located at the inner bottom of the reactor body 1 and below the aeration device 3.

[0038] An inner cylinder 8 is also provided in the reactor body 1. The upper port 81 of the inner cylinder 8 is higher than the top of the rea...

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Abstract

The invention discloses a deep-well aerobic digestive treatment device and a treating method for organic sludge. The device comprises a reactor main body and a top box, wherein air inlets of intake pipes for aeration and circulation both are connected to an air compressor; a sludge outlet of a sludge inlet pipe is located at the axial middle part of the reactor main body; an air outlet of the intake pipe for aeration is lower than the sludge outlet of the sludge inlet pipe; a sludge inlet of a sludge outlet pipe is located at the internal bottom of the reactor main body and located under an aeration device; the upper port of an inner barrel in the reactor main body is located in the top box and the bottom port of the inner barrel is located between the sludge outlet of the sludge inlet pipe and the air outlets of the intake pipes; the sludge inlet pipe and the intake pipe for aeration is located outside the inner barrel; the sludge outlet pipe and the intake pipe for circulation are located in the inner barrel; an exhaust device is arranged at the top of the top box; the sludge outlet pipe extends upwards out of the top box and the sludge outlet of the sludge outlet pipe is communicated with a flocculation floatation tank; and a vacuumizing device is arranged on the sludge outlet pipe between the top box and the flocculation floatation tank. The deep-well aerobic digestive treatment device is high in organic matter degradation and removal speed, few in volatile solids in treated sludge, low in aeration amount and energy consumption; and multiple purposes of the air are realized, so that the cost is saved.

Description

Technical field [0001] The invention relates to an organic sludge treatment device and a treatment method. Background technique [0002] With the popularization of sewage treatment facilities, the increase in treatment capacity, the improvement of treatment standards and the expansion of treatment functions, the amount of sludge produced will increase substantially. At present, according to the sewage treatment load rate of 75%, and 6 tons of sludge with a moisture content of 80% per 10,000 tons of sewage, it is estimated that my country will produce about 30 million tons of urban sewage sludge with a moisture content of 80% each year. According to forecasts, the sludge output will exceed 60 million tons per year by 2020. In Europe and America, sludge treatment infrastructure costs account for as much as 60% to 70% of the total infrastructure costs of sewage treatment plants. The treatment cost of surplus sludge accounts for 25%-40% of the operating cost of the sewage plant, ev...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/02
CPCY02W10/20
Inventor 于桂英孙钦凯李师松宫英杰马华飞梁彦娟
Owner 山东汇盛天泽环境工程有限公司
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