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Thermal decomposition treatment method for organic castoff

A technology of organic waste and treatment method, which is applied in the field of energy-saving pyrolysis treatment of organic waste, can solve problems such as hindering the popularization of pyrolysis technology, low energy utilization efficiency, and high energy consumption of pyrolysis devices, and achieve an increase in annual operating time, Significant energy-saving effect and reduced pyrolysis energy consumption

Inactive Publication Date: 2009-02-18
南京绿展能源有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the pyrolysis of organic waste requires a higher reaction temperature, otherwise the pyrolysis is incomplete and will have a greater impact on the product
The pyrolysis process commonly used at present often adopts indirect heat exchange with high-temperature flue gas. According to different raw materials, the temperature range of the heated flue gas is about 400-1000°C, and the temperature of the exhausted flue gas is also higher, at 300-800°C. range, the energy of the exhausted flue gas is discharged from the device without being fully utilized by the pyrolysis device, resulting in huge energy consumption and low energy utilization efficiency of the pyrolysis device, which greatly hinders the promotion of pyrolysis technology; on the other hand, due to the pyrolysis device Need to withstand high temperature and have special requirements for materials, which makes the device expensive and further hinders the promotion of pyrolysis technology

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Crushing 50t / d of organic waste for pyrolysis such as waste rubber and plastic, and sending the crushed organic waste for pyrolysis into the feeding port of the feeding device. The feeding device adopts a piston pusher.

[0020] The organic waste for pyrolysis is sent to the pre-pyrolysis device through the piston pusher. The pre-pyrolysis device adopts an externally heated screw conveyor with a hot air jacket, and performs indirect heat exchange with the flue gas in the hot air jacket while conveying the organic waste. Under normal pressure, the pre-pyrolysis time is 1 hour, and the reaction temperature in the pre-pyrolysis section is controlled at 200°C. After being heated, the organic waste undergoes pre-pyrolysis reactions such as drying and preliminary degradation. The waste gas produced in the pre-pyrolysis process is discharged from several waste gas outlets set on the top of the external heating screw conveyor in the pre-pyrolysis section.

[0021] The pre-py...

Embodiment 2

[0025] Send 100t / d of organic waste for pyrolysis such as sludge and oil sludge into the feeding port of the feeding device. The feeding device adopts screw conveyor.

[0026] The organic waste for pyrolysis is sent to the pre-pyrolysis device through the screw conveyor. The pre-pyrolysis unit adopts a scraper machine with a hot-air jacket to carry out indirect heat exchange between the organic waste and the flue gas in the hot-air jacket while conveying. Under normal pressure, the pre-pyrolysis time is 0.5 hour, and the reaction temperature in the pre-pyrolysis section is controlled at 100°C. After the organic waste is heated, it undergoes pre-pyrolysis reactions such as drying and preliminary decomposition. The waste gas generated in the pre-pyrolysis process is discharged from several waste gas outlets on the top of the scraper machine.

[0027] The pre-pyrolysis product enters the pyrolysis section from the material outlet at the tail of the scraper machine in the pre-p...

Embodiment 3

[0031] Sorting and crushing 200t / d domestic waste, the sorted and crushed organic domestic waste is sent to the feeding port of the feeding device. The feeding device adopts scraper machine.

[0032] The organic waste for pyrolysis is sent to the pre-pyrolysis device through the scraper machine. The pre-pyrolysis unit adopts an externally heated piston pusher with a hot air jacket, and performs indirect heat exchange with the flue gas in the hot air jacket while conveying the organic domestic waste. Under normal pressure, the pre-pyrolysis time is 0.1 hour, and the reaction temperature in the pre-pyrolysis section is controlled at 400°C. After being heated, the organic waste undergoes pre-pyrolysis reactions such as drying and preliminary degradation. The waste gas produced in the pre-pyrolysis process is discharged from several waste gas outlets set on the top of the externally heated piston pusher in the pre-pyrolysis section.

[0033] The pre-pyrolysis product enters the...

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Abstract

The invention relates to an organic waste pyrolytic treatment method. In the prior art, the energy consumption is high; the cost is large; and the service life of equipment is short. The organic waste pyrolytic treatment method adopts the pyrolytic treatment technique of combination of a pre-pyrolysis section and a secondary pyrolytic section to reutilize heating flue gas exhausted by the pyrolytic section for heating the pre-pyrolysis section according to a two-stage mechanism of pyrolysis. The method comprises the following steps: firstly, organic waste for pyrolysis is crushed according to the feeding demand; secondly, the crushed organic waste for pyrolysis is sent into a pre-pyrolysis device for drying and primary degradation; and thirdly, pre-pyrolysis products are sent into a pyrolytic device for pyrolysis, and oil products, fuel gas and carbon residue generated by the reaction are respectively exhausted. The pyrolytic device is heated through a hot-blast stove and tail gas exhausted by the hot-blast stove is sent into a hot-blast jacket of the pre-pyrolysis section for heating the pre-pyrolysis section section. The organic waste pyrolytic treatment method fully utilizes the caloric content of the flue gas, has obvious energy-saving effect, saves the consumption of high-quality steels and improves the service life of the pyrolytic device.

Description

technical field [0001] The invention belongs to the technical field of organic matter treatment, and the method relates to an organic waste treatment method, in particular to an energy-saving pyrolysis treatment method of organic waste. Background technique [0002] The disposal of organic waste should be based on the principles of recycling, reduction, and harmlessness. In today's social environment where the green GDP continues to grow and the harmonious development of the economy and the environment is advocated, it is imperative to comprehensively treat organic waste as a resource, and energy conservation and emission reduction are increasingly valued in my country. There are many types of organic waste, such as plastic, rubber, bamboo, wood, fabric, sludge, straw, municipal solid waste, oil sludge, waste oil, organic waste liquid, etc. If they are directly incinerated, their heat energy is simply used, and energy utilization The form is single, and it will cause seriou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): A62D3/40A62D101/20
Inventor 马加德张志霄
Owner 南京绿展能源有限公司
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