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Surplus biochemical sludge reduction treatment system and treatment method

A treatment system, biochemical sludge technology, applied in sludge treatment, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve the problems of occupying a large amount of land, harsh reaction conditions, soil heavy metal pollution, etc.

Active Publication Date: 2021-08-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

These technologies have a certain effect on the reduction of excess activated sludge, but they all have obvious shortcomings. For example, the dry landfill technology not only occupies a large amount of land, but also has the risk of polluting groundwater, and the composting technology will cause heavy metals in the soil during use. Pollution and biological pollution, incineration technology not only requires high equipment and high processing costs, but also produces harmful gases that pollute the atmosphere
[0004] For example, CN105859088A discloses a supercritical sludge treatment system and method, which makes the sludge slurry undergo a combustion reaction in the reactor of the supercritical sludge treatment device by adding oxidant and carbon-containing organic powder, but the reaction conditions are very harsh

Method used

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  • Surplus biochemical sludge reduction treatment system and treatment method

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specific Embodiment approach

[0065] According to a specific embodiment of the present invention, the method for mixing, heating and boosting the remaining biochemical sludge and additives in the feed system includes:

[0066] Send the excess biochemical sludge and additives through the excess biochemical sludge inlet and additive inlet respectively, or send the excess biochemical sludge and additives into the raw material buffer tank 2 through the excess biochemical sludge inlet, and set it in the raw material buffer The heater 6 in the tank 2 heats the reaction material to 80-300°C, preferably 100-250°C, and then boosts the feed to 0.05-10MPa, preferably 0.1-5MPa, through the feed booster pump 5, and sends it to into the reaction system for subtractive reaction.

[0067] According to another specific embodiment of the present invention, the method for mixing, heating and boosting the remaining biochemical sludge and additives in the feed system includes:

[0068] Send the remaining biochemical sludge in...

Embodiment 1

[0082] This example is used to illustrate the method for sludge reduction treatment using the excess biochemical sludge treatment system of the present invention.

[0083] Such as figure 1 As shown, the remaining biochemical sludge treatment system includes a feed system, a reaction system and a separation system.

[0084] The method of mixing, heating and boosting the sludge raw material (the temperature of the sludge raw material is at room temperature 35°C) and alkaline additives in the feed system includes: sending the sludge raw material into the raw material buffer tank through the remaining biochemical sludge inlet Inside. The reaction material is drawn out after being buffered by the raw material buffer tank, and sent to the feed booster pump together with the alkaline additive (aqueous sodium hydroxide solution, the concentration of which is 65% by mass) to boost the pressure to 1.5MPa, and is heated to 180°C by a heater , sent to the reaction system for subtractive...

Embodiment 2

[0088] This example is used to illustrate the method for sludge reduction treatment using the excess biochemical sludge treatment system of the present invention.

[0089] According to the method of Example 1, the sludge reduction treatment is carried out on the sludge raw material. The structure and reaction conditions of the reactor used are the same as those in Example 1. The difference is that the reaction system also includes a steam flash tank. The reaction product used in the second outlet is decompressed and then enters the steam flash tank for flash evaporation. The operating pressure of the flash tank is 0.1MPa, the temperature after flash evaporation is 120°C, and the vaporization rate is 10%. The steam generated is directly used as the fuel of the reaction system The heat source is evenly distributed by the gas distributor through the heat source inlet, and then sent to the raw material buffer tank 2 of the feeding system for contact, mixing and heat exchange with t...

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Abstract

The invention relates to the application field of solid waste reduction and resource utilization, and discloses a residual biochemical sludge reduction treatment system and a treatment method, wherein the treatment system includes: a feeding system, a reaction system and a separation system, and the The reaction system includes: a reactor and a pressure reducer; the reactor includes: a pressure reducing device, a partition plate and an internal mixer which are sequentially arranged from bottom to top along its height direction, and the partition plate divides the reactor into two upper and lower parts The reaction zone, the internal mixer communicates with the lower reaction zone of the reactor through the partition plate, and the internal mixer is also provided with a reaction product outlet communicated with the upper reaction zone of the reactor; the reactor is also provided with an external circulation device. Using the treatment system of the present invention to perform hydrothermal treatment on the surplus activated sludge can effectively remove the organic matter in the sludge, obtain the surplus sludge with greatly reduced water content, and realize the reduction of sludge discharge.

Description

technical field [0001] The invention relates to solid waste reduction and resource utilization, and more specifically, to a residual biochemical sludge reduction treatment system and treatment method. Background technique [0002] In recent years, my country's environmental protection industry has developed rapidly, and the sewage treatment capacity and treatment rate have increased rapidly. As of the end of September 2016, a total of 3,976 sewage treatment plants have been built nationwide, with a daily sewage treatment capacity of 170 million cubic meters. It plays a big role. But at the same time, the sewage treatment process produces a large amount of excess activated sludge. Based on the amount of excess activated sludge produced by the current sewage treatment, 1.3 million cubic meters of excess activated sludge with a water content of 98% by weight will be produced every day, with an annual output of excess activated sludge. Sludge will reach 475 million cubic meters,...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F11/00C02F11/18
CPCC02F11/00C02F11/18C02F2303/06
Inventor 秦娅袁清毛俊义朱振兴唐晓津桑军强
Owner CHINA PETROLEUM & CHEM CORP
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