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Method for regulating and controlling flue gas temperature of flue and negative pressure of hearth in reduction stage of anode furnace

A technology of flue gas temperature and furnace negative pressure, which is applied in the field of regulating flue gas temperature and furnace negative pressure in the reduction stage of the anode furnace, and can solve the problem of heavy maintenance and repair work of boiler rapping facilities, steam drums, and water walls, which affect the anode Furnace production operation planning operation, waste heat boiler occupies a large area and other problems, to achieve the effect of stable flue gas cooling and dust removal process, less occupied area and long running time

Active Publication Date: 2021-11-30
BAIYIN NONFERROUS GROUP
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In the reduction stage of the anode furnace, natural gas, pulverized coal or heavy oil and other reducing agents need to be introduced to carry out the reduction operation. During the reduction period, the temperature of the flue gas in the furnace generally reaches 1300-1400 ° C. In the face of high-temperature flue gas, different manufacturers adopt different methods. Flue gas cooling and dust reduction methods are used for treatment. Among them, some enterprises use the "secondary combustion chamber + waste heat boiler" cooling and dust collection method for flue gas cooling and dust collection. However, production practice has proved that this method has the following problems: (1 ) The waste heat boiler occupies a large area and has a relatively complex structure. The maintenance and repair workload of the boiler rapping facilities, steam drum, and water wall is relatively large, and the ash accumulation in the furnace of the boiler radiation part must be cleaned regularly, which consumes a lot of manpower and material resources. High maintenance and operation costs
(2) The waste heat boiler system needs to carry out regular maintenance work on the boiler body for a certain period of time, and the maintenance time is generally 1-2 days. If the anode furnace production plan density is high, and it coincides with the boiler body maintenance, it will affect the overall production of the anode furnace The planned operation of the operation will affect the overall production capacity of the anode furnace

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  • Method for regulating and controlling flue gas temperature of flue and negative pressure of hearth in reduction stage of anode furnace

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Embodiment

[0017] Such as figure 1 , this embodiment provides a method for controlling flue gas temperature and furnace negative pressure in the reduction stage of the anode furnace. The temperature generally reaches 1300-1400°C. In the face of high-temperature flue gas, the method of "secondary combustion chamber + flue gas spraying device" is used for flue gas cooling and dust collection, including rotary anode furnace body, zigzag flue, secondary Secondary combustion chamber, spray device, concrete method comprises the following steps:

[0018] (1) The outlet end of the rotary anode furnace body is connected to the secondary combustion chamber through a zigzag flue. During the reduction stage of the anode furnace body, the dilution air flow in the secondary combustion chamber is adjusted to control the flow within a constant flow range. Reduce the flue gas temperature to less than 800°C at the outlet of the secondary combustion chamber;

[0019] (2) A spraying device is connected to...

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Abstract

The invention discloses a method for regulating and controlling flue gas temperature of a flue and negative pressure of a hearth in a reduction stage of an anode furnace, and belongs to the technical field of copper smelting. The method comprises a rotary anode furnace body, a Z-shaped flue, a secondary combustion chamber and a spraying device. The method comprises the following steps of (1) connecting the outlet end of the rotary anode furnace body with the secondary combustion chamber through the Z-shaped flue, and reducing the flue gas temperature at the outlet of the secondary combustion chamber to be within 800 DEG C; (2) connecting the spraying device to the outlet end of the secondary combustion chamber, and spraying atomized cooling water to the top of the spraying device; and (3) calculating the amount of atomized cooling water sprayed by the top of the spraying device. According to the method, the investment, maintenance and human costs of equipment and facilities are saved, the continuous service cycle of high-temperature flue gas collecting equipment of the furnace body is prolonged, clean production is realized, the furnace is not stopped, the production is not influenced, the flue gas temperature in the reduction stage of the anode furnace is controlled within a reasonable range of production requirements, and the overall regulation and control of the negative pressure of the furnace body and the hearth are not influenced.

Description

technical field [0001] The invention relates to the technical field of copper smelting, in particular to a method for regulating flue gas temperature and furnace negative pressure in the reduction stage of an anode furnace. Background technique [0002] With the continuous improvement of the production capacity of copper smelting enterprises, most copper smelting enterprises currently use rotary anode furnaces for anode copper refining production in the refining process. In the reduction stage of the anode furnace, natural gas, pulverized coal or heavy oil and other reducing agents need to be introduced to carry out the reduction operation. During the reduction period, the temperature of the flue gas in the furnace generally reaches 1300-1400 °C. In the face of high-temperature flue gas, different manufacturers adopt different methods. Flue gas cooling and dust reduction methods are used for treatment. Among them, some enterprises use the "secondary combustion chamber + wast...

Claims

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Application Information

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IPC IPC(8): C22B15/00
CPCC22B15/0039
Inventor 张智汇王鲁博刘兴奎卢卫宁赵鲁肖翔郭玉龙
Owner BAIYIN NONFERROUS GROUP