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Anaerobic reaction system for sewage and anaerobic treatment method for sewage

An anaerobic reaction and anaerobic reactor technology, which is applied in the field of sewage anaerobic reaction system and its anaerobic treatment, can solve the problem of increasing the construction cost and construction time of biogas projects, low practical application value of biogas projects, and ineffective pollutants. Degradation and other problems, to achieve the effect of improving environmental conditions, increasing rate, and increasing activity

Inactive Publication Date: 2013-04-03
湘潭秋水环境技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Therefore, in order to increase the biogas production, the scale of the biogas project is made very large, which virtually increases the construction cost and construction time of the biogas project; at the same time, because the anaerobic reaction is greatly affected by the temperature, the efficiency of the anaerobic reaction varies from high to low , the main pollutants in the sewage cannot be effectively degraded, resulting in the discharge is still difficult to meet the standards
[0003] In the prior art, in order to improve the efficiency of the anaerobic reaction, the measures of heating and insulating the sewage have been taken. However, the heating and insulating of the sewage in the prior art requires a large amount of energy consumption, especially when the temperature is low. Even if all the biogas produced by the anaerobic reaction is used to heat the sewage, it cannot meet the demand
Therefore, the actual application value of the biogas project is low

Method used

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  • Anaerobic reaction system for sewage and anaerobic treatment method for sewage
  • Anaerobic reaction system for sewage and anaerobic treatment method for sewage
  • Anaerobic reaction system for sewage and anaerobic treatment method for sewage

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Embodiment 1

[0035] combine figure 1 , a sewage anaerobic reaction system, including a sewage collection tank 1, an anaerobic reactor 2 and a biogas storage tank 3 connected in sequence, and a heat recovery device 4 and a heat recovery device 4 are sequentially connected between the sewage collection tank 1 and the anaerobic reactor 2 The heat exchanger 5 and the heat recovery device 4 are provided with a heat exchange tube 6, the water outlet of the anaerobic reactor 2 is connected to the water inlet of the heat exchange tube 6, and the water outlet of the heat exchange tube 6 is connected to the next water treatment process;

[0036] The anaerobic reaction system also includes a heating device, the heating device includes a boiler 7 and a temperature control device, the boiler 7 is connected with a first circulating cooling pipe 8 and a second circulating cooling tube 10, and the first circulating cooling tube 8 is arranged in the heat exchanger 5 , the second circulating heat pipe 10 is...

Embodiment 2

[0051] combine figure 2 , image 3 , Figure 4 , a sewage anaerobic reaction system, including a sewage collection tank 1, an anaerobic reactor 2 and a biogas storage tank 3 connected in sequence, and a heat recovery device 4 and a heat recovery device 4 are sequentially connected between the sewage collection tank 1 and the anaerobic reactor 2 The heat exchanger 5 and the heat recovery device 4 are provided with a heat exchange tube 6, the water outlet of the anaerobic reactor 2 is connected to the water inlet of the heat exchange tube 6, and the water outlet of the heat exchange tube 6 is connected to the next water treatment process;

[0052] The anaerobic reaction system also includes a heating device, the heating device includes a boiler 7 and a temperature control device, the boiler 7 is connected with a first circulating cooling pipe 8 and a second circulating cooling tube 10, and the first circulating cooling tube 8 is arranged in the heat exchanger 5 , the second c...

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Abstract

The invention discloses an anaerobic reaction system for sewage and an anaerobic treatment method for sewage. The anaerobic reaction system comprises a sewage collection pool, an anaerobic reactor and a biogas storage tank which are sequentially connected, wherein a heat recoverer and a heat exchanger are sequentially connected between the sewage collection pool and the anaerobic reactor, a heat exchange tube is arranged in the heat recoverer, the water outlet of the anaerobic reactor is connected with the water inlet of the heat exchange tube, and the water outlet of the heat exchange tube is connected with the next water treatment procedure. The anaerobic reaction system further comprises a heating device, wherein the heating device comprises a boiler, a circulating heat dissipation tube and a temperature control device used for automatically controlling the heating temperature of sewage in the heat exchanger and the anaerobic reactor. The anaerobic reaction system for sewage and the anaerobic treatment method for sewage disclosed by the invention have the advantages that the process flow is simple, the biogas yield is high, the energy consumption is low, and moreover, the anaerobic reaction system for sewage is low in construction cost.

Description

technical field [0001] The invention relates to the technical field of organic wastewater treatment, in particular to a sewage anaerobic reaction system and an anaerobic treatment method thereof. Background technique [0002] Wastewater containing high concentrations of organic matter, such as common human and animal manure, food processing wastewater, straw retting, etc., is mainly treated through biogas engineering. The purpose is to decompose organic matter and generate biogas through anaerobic fermentation, which not only eliminates pollution but also obtains Energy (biogas) and organic fertilizers. However, in the actual operation of the biogas project, due to its inherent defects, it has not played its due role, such as low gas production rate and difficult discharge standards. This is mainly because the anaerobic reaction is sensitive to temperature and temperature changes. Only at a relatively high temperature (38°C) and a small temperature difference range (35-40°C...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/28C12M1/107C12M1/02C12M1/38C12P5/02
CPCY02E50/343C12M41/24C12M23/36C12M41/12C12M21/04Y02E50/30Y02P20/59
Inventor 蒋作佩曾晓屏钟靓杰
Owner 湘潭秋水环境技术有限公司
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