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System and method for supercritical water oxidation treatment and resource utilization of organic sludge

A technology of supercritical water oxidation and organic sludge, applied in chemical instruments and methods, water/sludge/sewage treatment, sludge treatment, etc., can solve the problem of high transportation cost, large one-time investment, and few disposal process links, etc. problems, to achieve the effect of high power generation efficiency and major social benefits

Inactive Publication Date: 2012-06-20
NANJING UNIV OF TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There are two main methods for sludge incineration: one is direct incineration of dewatered sludge, which has few process links and simple process, but consumes a lot of fuel and has high operating and transportation costs; Dewatered sludge is incinerated after drying or semi-drying treatment. Although it can make incineration relatively simple and reduce transportation costs, it requires supporting drying equipment, resulting in higher drying costs.
The incineration of sludge was once very popular, but the one-time investment is large, the operating cost is high, and the flue gas and incineration ash need to be reprocessed because the organic matter will produce dioxin and other highly toxic substances when the combustion temperature is lower than 850 ° C. Disadvantages limit its application
When the landfill method is used, the various toxic and harmful substances contained in the sludge will pollute the groundwater and the atmosphere through the erosion and leakage of rainwater. Increasingly limited and costly to transport over long distances
Sludge can be used in agriculture after being treated by composting, but direct application of pathogens and toxic and harmful substances contained in sludge to agriculture will cause secondary pollution of soil and water bodies, and there are still limitations in the case of immature related technologies sex

Method used

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  • System and method for supercritical water oxidation treatment and resource utilization of organic sludge
  • System and method for supercritical water oxidation treatment and resource utilization of organic sludge
  • System and method for supercritical water oxidation treatment and resource utilization of organic sludge

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0038] Such as figure 1 The supercritical water oxygen treatment and resource utilization system of organic sludge includes grid 1, sludge mixing crusher 2, sludge pressure pump 3, preheater 4, supercritical water oxidation reactor 5, oxidant pressure Pump 7, high pressure hydrocyclone 8 and supercritical generator set 9. Grille 1, sludge mixing crusher 2, sludge pressure pump 3 and preheater 4 are connected sequentially through the delivery pipeline, the output port of preheater 4 is connected to the input port 51 of supercritical water oxidation reactor, and the oxidant pressure pump 7 is connected to the oxidant input port 52 of the supercritical water oxidation reactor 5. A heater 6 is installed in the supercritical water oxidation reactor. The output port 53 of the supercritical reactor is connected to the inlet of the high-pressure hydrocyclone 8, the fluid outlet of the high-pressure hydrocyclone 8 is connected to the supercritical generator set 8, and the output por...

Embodiment 2

[0049] Such as figure 2 As shown, the difference between this embodiment and Embodiment 1 is that the power generation system is composed of a steam turbine 10, a steam generator set 11, a cold water pump 12, a grid D, a heating device E and a refrigeration device F; the steam turbine 10 high-temperature steam outlet and The input end of the steam generating set 11 is connected, and the output of the steam generating set 11 is connected to the power grid D in sequence; the 10 high-temperature steam outlets of the steam turbine are respectively connected to the heating device E and the cooling device F; the cold water pump 12 passes through the pipeline and the high-pressure hydrocyclone 8 Supercritical water outlet connection. The supercritical water discharged from the high-pressure hydrocyclone 8 is not used for supercritical power generation, but is turned into steam by adding cold water G to reduce the temperature and pressure, and then use the steam turbine to generate e...

Embodiment 3

[0060] Such as image 3 As shown, the difference between this embodiment and Embodiment 1 is that a heater 12 is provided at the supercritical water outlet of the high-pressure hydrocyclone 8 and the input of the supercritical generator set, and the supercritical water discharged from the high-pressure hydrocyclone 8 is not Directly perform supercritical power generation, but continue heating through the heater 12 to make the temperature reach above 580°C and the pressure at 30~40MPa, and then use it for supercritical power generation, so as to further improve the power generation efficiency, and use the back pressure steam after power generation For heating or cooling.

[0061] The method for supercritical water oxygen treatment and resource utilization of organic sludge comprises the following steps:

[0062] (1) Use the grid 1 to perform coarse filtration of the sludge to be treated to remove the large pieces and strips;

[0063] (2) Use the sludge stirring crusher 2 to f...

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Abstract

The invention relates to a system and a method for supercritical water oxidation treatment and resource utilization of organic sludge. The system for supercritical water oxidation treatment and resource utilization of the organic sludge comprises a grid, a sludge stirring and crushing machine, a sludge pressure pump, a preheater, an oxidizing agent pressure pump, a supercritical water oxidation reactor, a high-pressure hydrocyclone separator and a power generation system, wherein the grid, the sludge stirring and crushing machine, the sludge pressure pump and the preheater are sequentially connected through a delivery pipeline; an output port of the preheater is connected to an input port of the supercritical water oxidation reactor; the oxidizing agent pressure pump is connected to an oxidizing agent input port of the supercritical water oxidation reactor; a heater, a supercritical water input port of the supercritical water oxidation reactor, and the high-pressure hydrocyclone separator are arranged in the supercritical water oxidation reactor; and an output port of supercritical water of the high-pressure hydrocyclone separator is connected with an input end of the power generation system.

Description

technical field [0001] The invention relates to a system and method for supercritical water oxidation treatment and resource utilization of organic sludge. Specifically, the supercritical water oxidation method is used to treat organic sludge and convert harmful organic components into water and carbon dioxide. And a small amount of stable inorganic substances and other substances, while using waste heat to generate electricity, while achieving the goal of "reduced, stable, and harmless" sludge treatment, it also realizes comprehensive utilization of energy. Background technique [0002] With the acceleration of urbanization and the improvement of environmental protection standards, the rate and degree of sewage treatment are also increasing and deepening, and the output of sludge is also greatly increased. Organic sludge is the product of wastewater treatment (including domestic wastewater and industrial wastewater), which contains a large amount of toxic and harmful substa...

Claims

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Application Information

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IPC IPC(8): C02F11/06C02F11/18C02F11/00F01D15/10C02F101/30
Inventor 廖传华周玲郭丹丹朱跃钊陈海军张阔武一鸣杨丽
Owner NANJING UNIV OF TECH
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