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Method and device for producing methane by using dry anaerobic digestion for urban sludge and organic matter

A dry anaerobic and municipal sludge technology, applied in the field of solid waste recycling, can solve the problems of difficult gas overflow, difficult mass transfer, and difficult enrichment of methane bacteria, so as to facilitate enrichment, facilitate operation and management, and save The effect of temperature control on energy consumption

Active Publication Date: 2010-12-22
TONGJI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The purpose of the present invention is to overcome the difficulties of mass transfer, difficult enrichment of methane bacteria and difficulty of gas overflow due to the characteristics of high viscosity, no fluidity, and no void ratio in the dry fermentation process of municipal sludge, and overcome other dry fermentation methods. The shortcoming that the equipment cannot achieve efficient microscopic mixing of sludge provides a method and device for producing biogas by dry anaerobic fermentation of municipal sludge and organic matter

Method used

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  • Method and device for producing methane by using dry anaerobic digestion for urban sludge and organic matter
  • Method and device for producing methane by using dry anaerobic digestion for urban sludge and organic matter
  • Method and device for producing methane by using dry anaerobic digestion for urban sludge and organic matter

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Embodiment 1

[0033] Such as Figure 1-3 As shown, the device is composed of a fermentation tank body, a stirring system, a temperature control and heat preservation system, and a control system; the fermentation tank body 6 lies on the support 12, the bearing and the bearing support 1 are fixed on the support 12, and the rotating shaft 8 passes through the fermentation Tank body 6, one end of the rotating shaft 8 is connected to the bearing and bearing support 1, the other end is connected to the coupling 9, the coupling 9 is connected to the transmission 10, the transmission 10 is connected to the motor 11; the fermentation tank body 6 is provided with a feeding port 5 and a discharge port 13. The sludge sampling port 14 and the gas sampling port 3, the gas enters the wet bulb gas flow meter 19 after the rotameter 18; the tank is equipped with a stirring system, which is composed of a rotating shaft 8, an outer spiral annular belt 4 and an inner spiral annular belt 15. , The outer spiral r...

Embodiment 2

[0036] Take 300L of dewatered sludge from sewage plant B, put it into the fermentation tank through the feed port 5, and mix it with the last batch of fermented biogas residue. At this time, the material height is about 5cm higher than the upper edge of the outer spiral belt 4; The moisture content of the material is 80.8%, the organic content is 56.2%, the C / N ratio is 9.8, and the material adhesion is 45g; the feed inlet 5 is sealed, the stirring speed is set to 12r / min, the motor switch is turned on, and the fermentation starts; start 3 Days later, the temperature of the material measured by the temperature display device is 34℃, and the wet gas flow meter shows the gas output as 20L; turn on the temperature control device, set the temperature to 35℃, adjust the stirring speed to 20r / min, and set the stirring motor to turn on for 1 hour / Stop operation for 1 hour; after 8 days of operation in this stage, the water content of the material measured from the sludge sampling por...

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Abstract

The invention belongs to the field of reclamation of solid wastes, in particular relating to a method and a device for producing methane by using a dry anaerobic digestion for urban sludge and an organic matter. The device comprises a reaction chamber and a double-layer helix ribbon type agitator and is provided with a feed inlet and outlet, a sample port, a temperature-setting controller, a methane metering device, a stirring control device and others devices. The method comprises the following steps: dewatering sludge is placed into a fermentation tank for inoculation and seal, the revolving speed at start-up stage is 5-15r / min and daily stirring time is 12h, the revolving speed at acid-producing stage is 10-20r / min, intermittent operation is carried out; the daily stirring time is more than or equal to 8h and less than or equal to 16, and starting and stopping frequency for the motor is required to be increased; temperature control is performed at acid-producing stage and methane-producing stage and material temperature is controlled to be 35+ / -1 DEG C; and after finishing the fermentation, one fourth to one third of biogas residues are left for being used as inoculum for the next batch of fermented materials and the rest of residues are discharged. The invention can be applied to reclamation treatment of the urban sludge and can obviously save equipment investment and land occupation compared with the wet fermentation.

Description

Technical field [0001] The invention belongs to the field of solid waste resource recovery, and specifically relates to a method and device for dry anaerobic fermentation of urban sludge and organic matter (such as livestock manure, food waste, etc.) to produce biogas. Background technique [0002] The amount of dewatered sludge produced by the purification of domestic sewage in urban sewage treatment plants is huge, and the current annual collection capacity is about 26 million tons. The sewage treatment plants mostly use concentrated dewatering for landfilling after treatment and disposal. The method not only occupies limited land resources, but also easily causes secondary pollution. In addition, cities produce a large amount of organic waste, such as livestock manure, food waste, etc. The resource utilization rate of these waste landfills is low, which is not in line with the principle of sustainable development in my country. In recent years, the global energy stru...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/04C12P7/40C12P5/02C12M1/38C12M1/107
CPCC12M21/16Y02E50/343C12M29/18C12M21/04C12M27/06Y02E50/30
Inventor 戴晓虎董滨吴星五李国建周增炎高廷耀
Owner TONGJI UNIV
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