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Bi-circulating multistage anaerobic reaction device

An anaerobic reaction device and anaerobic reactor technology, applied in anaerobic digestion treatment, waste fuel and other directions, can solve the problems of high energy consumption of carrier flow, high system design requirements, low processing efficiency, etc., and achieve fast start-up speed , saving land, good water output effect

Active Publication Date: 2014-09-03
广西绿晨环境工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The patented reactor can still form an internal circulation, but the structure is greatly simplified, the clogging problem is effectively alleviated, and the introduction of the carrier solves the problem of low ascending flow rate
However, the disadvantages of this patent are: the carrier current consumes a lot of energy, and the design requirements of the system are high
[0005]2. Application number: 200610122737.6, invention name: two-phase integrated multi-level internal circulation anaerobic bioreactor, the reactor is equipped with multi-layer internal circulation technology device , so that the fluid is in a good fluidized state. Compared with the traditional anaerobic reactor, its treatment effect has the following advantages: small footprint; high load rate, strong impact load resistance, high treatment efficiency, stable operation treatment effect, etc.; but The disadvantages of this patent are: the lack of external circulation, the pH value needs to be adjusted for wastewater with high difficulty and low pH value, and the operating cost is high
However, the disadvantage of this patent is that it lacks external circulation, and the pH value needs to be adjusted for wastewater with high difficulty and low pH value, and the operating cost is high.
However, the disadvantages of this patent are: the start-up speed of the device is slow, the treatment efficiency is not high, and the external circulation is lacking. For the wastewater with high difficulty and low pH value, the pH value needs to be adjusted, and the operating cost is high.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Such as figure 1As shown, a double-cycle multi-stage anaerobic reaction device includes a two-stage anaerobic reactor, and the anaerobic reactor includes a container body 15, and the container body 15 is sequentially provided with a water distributor 2 from bottom to top, leading to a distribution channel. The water inlet pipe 1 of the water tank 2, the first-level three-phase separator 3, the second-level three-phase separator 6, the outlet pipe 11 and the cyclone gas-liquid separator 10, and the top of the cyclone gas-liquid separator 10 is provided with a biogas outlet leading to the outside A fluidized bed reaction chamber 14 is provided between the pipe 8, the water distributor 2 and the primary three-phase separator 3, and a deep purification reaction chamber 4 is provided between the primary three-phase separator 3 and the secondary three-phase separator 6 , the upper cover of the first-level three-phase separator 3 is provided with a rising pipe 12 communicating...

Embodiment 2

[0039] The difference between this embodiment and Embodiment 1 is that the granular sludge 13 is elliptical with a long diameter of 0.5-3.0 mm; the primary three-phase separator 3 and the secondary three-phase separator 6 are composed of two rows of folding plates Composed in parallel, each row is provided with 10 folded plates 18, the top and bottom of the cyclone gas-liquid separator are conical, the conical surface and the plane form an angle of 60°, the rising pipe 12, the descending pipe 5 and the gas collecting pipe 7 The pipe diameter is 350mm.

Embodiment 3

[0041] The difference between this embodiment and Embodiment 1 is that the granular sludge 13 is spherical with a diameter of 0.5-2.0 mm and elliptical with a major diameter of 1.5-3.0 mm; the primary three-phase separator 3 and the secondary three-phase separator 6 are composed of two rows of folded plates 18 in parallel, and each row is provided with 15 folded plates 18. The top and bottom of the cyclone gas-liquid separator are conical, and the angle between the conical surface and the plane is 55°. The riser pipe 12 , The pipe diameters of downcomer 5 and air collecting pipe 7 are 200mm.

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Abstract

The invention discloses a double-cycle multi-stage anaerobic reaction device, which includes two anaerobic reactors, the anaerobic reactors include a container body (15), and the container body (15) is arranged sequentially from bottom to top. There are water distributor (2), water inlet pipe (1) leading to water distributor (2), primary three-phase separator (3), secondary three-phase separator (6), outlet pipe (11) and rotary Flow gas-liquid separator (10), the top of the cyclone gas-liquid separator (10) is provided with a biogas outlet pipe (8) leading to the outside, and a water distributor (2) and a three-phase separator (3) are provided A fluidized bed reaction chamber (14), a deep purification reaction chamber (4) is provided between the primary three-phase separator (3) and the secondary three-phase separator (6). The invention has both internal circulation and external circulation, and has the advantages of power saving, less sludge, high treatment volume load rate, space saving, strong impact load resistance, etc., and is suitable for high-concentration and low-concentration organic industrial wastewater.

Description

technical field [0001] The invention belongs to sewage treatment equipment, in particular to a double-cycle multi-stage anaerobic reaction device. Background technique [0002] High-concentration organic wastewater is a major industrial pollution source that is difficult to treat, with high COD concentration. Conventional high-concentration organic wastewater treatment equipment includes UASB anaerobic reactors, anaerobic biological filters, etc., all of which have problems such as large investment, high operating costs, and poor treatment effects. This technical bottleneck restricts the popularization and application of traditional wastewater treatment technologies . [0003] The following are the public documents we found about the anaerobic reaction device: [0004] 1. Application number: 02282323.9, utility model name: internal circulation anaerobic expanded bed / fluidized bed reactor, the main technical feature of this reactor is that the gas-liquid separation zone and...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F3/28
CPCY02E50/343Y02E50/30
Inventor 聂威李彪粟莹
Owner 广西绿晨环境工程有限公司
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