Multi-stage inner circulation anaerobic reactor

A technology of anaerobic reactor and anaerobic reaction zone, which is applied in the field of multi-stage internal circulation anaerobic reactor, can solve the problems of difficult separation of sludge and hydraulic retention time, high solid content of effluent, and imperfection, and achieve sedimentation. Condition optimization, enhanced mass transfer, and effects of large fluid circulation

Inactive Publication Date: 2008-10-29
牟秀元
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Problems solved by technology

[0002] The development history of anaerobic reactors can be divided into three typical stages: the first stage is represented by continuous stirring (CSTR), and the disadvantages are: it is difficult to separate the sludge from the hydraulic retention time, the treatment cycle is long, and the solid content of the effluent is high ; The second stage is represented by the upflow anaerobic sludge bed (UASB), which is better than the first generation reactor, but it is limited to the treatment of medium-high temperature and high-concentration organic wastewater; the third stage is the expanded granular sludge bed (ECSB ) and the internal circulation reactor (IC), further improving the performance of the reactor, but not perfect

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  • Multi-stage inner circulation anaerobic reactor
  • Multi-stage inner circulation anaerobic reactor
  • Multi-stage inner circulation anaerobic reactor

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Embodiment 1

[0019] See figure 2 , the pretreated waste water enters the water inlet pipe 7 through the control of the valve 93 and connects the solid-liquid separator 70, and the solid-liquid separator 70 is conical; the heavy solids collect at the bottom center of the solid-liquid separator 70 and are discharged through the control of the pipeline 9 and the valve 93 for further treatment. The easily degradable matter and suspended matter are connected to the first reaction zone 10 through the water distribution plate 91 and the water distribution inclined pipe 92, and the first reaction zone 10 is connected to the second reaction zone 20 through the gas collection reflection plate 90, and the second reaction zone 20 is connected to the third reaction zone through the gas collection reflection plate 90. The reaction area 30, the third reaction area 30 is connected to the fourth reaction area 40 through the gas collection reflection plate 90, the fourth reaction area 40 is connected to the...

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Abstract

The invention relates to a multi-stage internal circular anaerobic reactor which aims at solving the defects of existing anaerobic reactors, such as difficulty in separating the sludge and hydraulic retention time, long treatment period, high solid-containing content of effluent, and limit to the treatment of organic wastewater with medium and high temperature and high concentration. The anaerobic reaction zone of the reactor is arranged above three stages, each of which is provided with a riser pipe used for leading fluid to flow up to a gas-liquid separator at the top part through an air collection baffle-board, a recirculatory pipe used for leading the fluid to flow down to a solid-liquid separator at the bottom part and a water distributor used for leading the fluid to enter the anaerobic reaction zone to carry out fluid circulation. The reactor is easy to operate and manage, optimizes disposition conditions and improves biomass in the reactor. The full contact of wastewater and microbe strengthens the mass transfer between the wastewater and particle sludge and guarantees the normal operation of the reactor in larger volume load.

Description

technical field [0001] The invention relates to biochemical environment-friendly engineering technology, in particular to a multi-stage internal circulation anaerobic reactor. Background technique [0002] The development history of anaerobic reactors can be divided into three typical stages: the first stage is represented by continuous stirring (CSTR), and the disadvantages are: it is difficult to separate the sludge from the hydraulic retention time, the treatment cycle is long, and the solid content of the effluent is high ; The second stage is represented by the upflow anaerobic sludge bed (UASB), which is better than the first generation reactor, but it is limited to the treatment of medium-high temperature and high-concentration organic wastewater; the third stage is the expanded granular sludge bed (ECSB ) and the internal circulation reactor (IC) as representatives, further improved the performance of the reactor, but not perfect. Contents of the invention [0003...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/28
CPCY02E50/343Y02E50/30
Inventor 牟秀元
Owner 牟秀元
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