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Sludge treatment system and method thereof

一种污泥处理、污泥的技术,应用在污泥处理、生物污泥处理、水/污泥/污水处理等方向,能够解决污泥与臭氧不能充分接触、难大规模推广应用、臭氧投放比例高等问题,达到提高氧化效率、降低能耗、减少投加量的效果

Inactive Publication Date: 2014-03-26
NANJING DELEI SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, according to domestic and foreign technical indicators, 15-21KWh of electricity is required to produce 1kg of ozone. Even if industrialized oxygen is used instead of air as a raw material, 8KWh of electricity consumption is required. A 16kg / h ozone generator needs to consume 240-336KWh of electricity. Its equipment investment, power system configuration, and operating costs are all factors that have to be considered by sludge treatment owners
[0008] Therefore, the sludge treatment system in the prior art has the following disadvantages: the residence time of ozone after entering the reactor is short, the sludge and ozone cannot be fully contacted, the utilization rate of ozone is low, the proportion of ozone input is high, the energy consumption is high, and the operating cost High, it is difficult to promote and apply on a large scale

Method used

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  • Sludge treatment system and method thereof
  • Sludge treatment system and method thereof
  • Sludge treatment system and method thereof

Examples

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Embodiment 1

[0035] Such as figure 1 and figure 2 As shown, a sludge treatment system of the present invention is characterized in that: the sludge treatment system includes a pump 1 with a flow rate of 8m3 / h, an ozone generator, an ejector 2 and a pipeline connected sequentially through a pipeline Reactor 3, the ozone generating device is used to provide ozone into the pipeline reactor 3 to achieve sufficient contact between ozone and sludge.

[0036] The ejector 2 is a Venturi mixer.

[0037] Described ozone generator is provided with the oxygen generator 4 of 1 60L / min and the ozone machine 5 of 1 240g / h connected by pipeline;

[0038] There are four pipeline reactors 3, and the pipeline reactors 3 are connected in parallel or in series through pipelines;

[0039] The inner surface of the pipeline reactor 3 is coated with a catalyst that can catalyze ozone into hydroxyl radicals, further improving the oxidation efficiency of ozone.

[0040] The lower part of the pipe reactor 3 is p...

Embodiment 2

[0062] Such as figure 1 and figure 2 As shown, a sludge treatment system of the present invention is characterized in that: the sludge treatment system includes a pump 1, an ozone generating device, an ejector 2 and a pipeline reaction tube with a flow rate of 16m3 / h connected sequentially through pipelines. device 3, the ozone generating device is used to provide ozone into the pipeline reactor 3, realize sufficient contact between ozone and sludge, and realize solid-liquid separation at the same time.

[0063] Described ozone generator is provided with the oxygen generator 4 of 1 140L / min and the ozone machine 5 of 1 480g / h connected by pipeline;

[0064] There are 8 pipeline reactors 3, and the pipeline reactors 3 are connected in series in groups of 4, and then two groups are connected in parallel;

[0065] The inner surface of the pipeline reactor 3 is coated with a catalyst that can catalyze ozone into hydroxyl radicals, further improving the oxidation efficiency of o...

Embodiment 3

[0090] Such as figure 1 and figure 2 As shown, a sludge treatment system of the present invention is characterized in that: the sludge treatment system includes a pump 1, an ozone generating device, an ejector 2 and a pipeline reaction tube with a flow rate of 2m3 / h connected sequentially through pipelines. device 3, the ozone generating device is used to provide ozone into the pipeline reactor 3, realize sufficient contact between ozone and sludge, and realize solid-liquid separation at the same time.

[0091] Described ozone generator is provided with the oxygen generator 4 of 1 5L / min and the ozone machine 5 of 1 30g / h connected by pipeline;

[0092] There are four pipeline reactors 3, and the pipeline reactors 3 are connected in parallel or in series through pipelines;

[0093] The inner surface of the pipeline reactor 3 is coated with a catalyst that can catalyze ozone into hydroxyl radicals, further improving the oxidation efficiency of ozone.

[0094] The lower part...

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Abstract

The invention discloses a sludge treatment system and a method thereof, wherein the sludge treatment system comprises a pump, an ozone generation device, an ejector and a pipeline reactor which are orderly connected by pipes. The sludge treatment system comprises the following steps of: (1) when sludge water to be treated is conveyed to the ejector by the pump in a certain speed, a side inlet of the ejector generates negative pressure to suck ozone generated by the ozone generation device, the sludge water and the ozone are mixed to form a mixture; and (2) the mixture enters a pipe reactor by a pipe, and the mixture is fully contacted with a catalyst layer in the pipeline reactor, to carry out oxidation reduction reaction under catalysis of the catalyst. The sludge treatment system implements modularization production of a sludge deweighting treatment system, does not need to reconstruct a current sludge system, eliminates offensive odor of the sludge treatment system and an outward mud cake, reduces energy consumption in a production process, and reduces a sludge discharge total amount of the system.

Description

technical field [0001] The invention relates to the technical field of sludge treatment, in particular to a sludge treatment system and a method thereof. Background technique [0002] The biological activated sludge process is the most widely used and mature sludge treatment technology, with low investment and operation costs and stable treatment effect. However, there is a problem with the activated sludge method, that is, a large amount of excess sludge will be generated, and the transportation and treatment costs of excess sludge account for a large proportion of the total operating costs, and there are still many conditions and restrictions in the treatment. At present, my country's urban sludge treatment volume is about 30 billion m3 / a, and biochemical sludge with a water content of 98% is about 200 million m3 / a, and the remaining sludge output will still grow at an average annual rate of 15%. 10 million t / a and oil refinery, the annual production of hydrous sludge is ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F11/06
CPCC02F1/004C02F1/78C02F9/00C02F11/06C02F11/122C02F11/14C02F2201/007C02F2201/782C02F2203/006C02F2209/38C02F2303/02C02F2303/10Y02W10/30C02F11/02
Inventor 吴浩
Owner NANJING DELEI SCI & TECH
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