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Solid hazardous waste and liquid hazardous waste cooperative disposal incinerator and disposal method

A hazardous waste and co-processing technology, applied in the direction of combustion method, incinerator, combustion type, etc., can solve the problems of insufficient capacity of liquid waste, weak disposal capacity of liquid hazardous waste, single phase state, etc., and achieve improved disposal capacity and good combustion Temperature, stable and reliable effect

Pending Publication Date: 2020-05-15
台州市德长环保有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The invention provides an incinerator and treatment method for co-processing solid hazardous waste and liquid hazardous waste. Aiming at the problems of the existing rotary kiln incinerators in the disposal of hazardous waste, the disposal phase state is single and the disposal capacity of liquid hazardous waste is weak. The mixed furnace type with a relatively independent combustion zone can complement the advantages and disadvantages of the fluidized bed incinerator and the rotary kiln incinerator. The liquid is burned in the fluidized bed-combustion chamber, and the solid is burned in the rotary kiln. In the center, the corresponding materials are converted into gas phase substances and then enter the common secondary combustion chamber, which can solve the shortcomings of the original rotary kiln’s insufficient capacity to dispose of liquid waste, improve the disposal capacity of hazardous waste with different physical properties and cannot be mixed, and better control secondary combustion. The combustion temperature of the combustion chamber makes the system run stably and reliably

Method used

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  • Solid hazardous waste and liquid hazardous waste cooperative disposal incinerator and disposal method
  • Solid hazardous waste and liquid hazardous waste cooperative disposal incinerator and disposal method
  • Solid hazardous waste and liquid hazardous waste cooperative disposal incinerator and disposal method

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Embodiment Construction

[0046] Such as figure 2 As shown, an incinerator for the co-combustion of solid and liquid hazardous wastes. The present invention adds a fluidized bed special for waste liquid incineration on the basis of the traditional rotary kiln one-chamber and two-chamber incinerator system. The combustion chamber shares the second combustion chamber with the first combustion chamber of the rotary kiln to form a hazardous waste incineration system with a rotary kiln and a fluidized bed combustion chamber.

[0047] The cooperative combustion device of the present application includes a rotary furnace, a combustion chamber 1, a fluidized bed, a combustion chamber 5, and a second combustion chamber 2. The furnace of the first combustion chamber 1 of the rotary kiln is provided with an inlet, a combustion-supporting air inlet of the rotary kiln and a flue gas outlet. The inlet is connected to a solid waste feeder 12, and the combustion-supporting air inlet of the rotary kiln is connected to a s...

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Abstract

The invention discloses a solid hazardous waste and liquid hazardous waste cooperative disposal incinerator and a disposal method. The solid hazardous waste and liquid hazardous waste cooperative disposal incinerator comprises a first rotary kiln combustion chamber, a first fluidized bed combustion chamber, a second combustion chamber and a rear smoke channel. The first rotary kiln combustion chamber is provided with a feed port, a rotary kiln combustion-supporting air inlet and a waste gas outlet. The first fluidized bed combustion chamber is provided with a fluidized air inlet and a waste gas outlet. A hearth of the first fluidized bed combustion chamber is filled with a quartz sand bed material. A waste liquid spraying device is arranged on the upper side of the quartz sand bed material. The fluidized air inlet is connected with a fluidization draught fan. The waste liquid spraying device is externally connected with a waste liquid pump. The second combustion chamber is provided with two waste gas inlets, a secondary air inlet and a waste gas outlet. The two waste gas inlets are connected with the waste gas outlet of the first rotary kiln combustion chamber and the waste gas outlet of the first fluidized bed combustion chamber correspondingly. Liquid is incinerated in the first fluidized bed combustion chamber, solid is incinerated in a rotary kiln, the corresponding materials are converted into gas-phase substances in the first combustion chambers, and then the gas-phase substances enter the common second combustion chamber, so that the problem that the liquid waste disposal capacity of an existing rotary kiln is not sufficient can be solved.

Description

Technical field [0001] The invention relates to the technical field of hazardous waste treatment, in particular to an incinerator and a treatment method for co-processing solid hazardous waste and liquid hazardous waste. Background technique [0002] With the development of society and economy, the number and types of industrial wastes, especially hazardous wastes, continue to increase, which has attracted great attention from the government and the public. The local discharge and unreasonable disposal of hazardous waste will endanger people's health, and long-term accumulation will severely damage the ecological environment on which mankind depends, and the extent of damage is much greater than that of domestic waste. Hazardous waste has become a prominent public hazard worldwide. Actively develop new technologies, new processes, and new equipment, carry out centralized management and comprehensive disposal of hazardous waste, and reduce and eliminate its pollution. [0003] Rota...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F23G5/16F23G5/027F23G5/12F23G5/20F23G5/30F23G5/44F23G5/46F23G7/00F23J15/00F23C10/18F23C10/20
CPCF23G5/16F23G5/12F23G5/027F23G5/30F23G5/20F23G7/008F23G5/46F23G5/446F23J15/006F23C10/20F23C10/18F23G2201/40F23G2202/103F23G2203/20F23G2203/50F23G2204/103F23G2209/10
Inventor 陈景波魏玺郑顺富郑存进付晓东邹铁凡宦仁福马周飞
Owner 台州市德长环保有限公司
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