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Coke oven raw gas heat continuous recovery system

A recovery system and waste gas technology, which are applied in the heating, coke oven, energy input and other directions of coke ovens, can solve the problem of water leakage from the coke oven riser pipe to the coke oven carbonization chamber, the complex composition of coke oven waste gas, and the impact on the safe production of coke ovens. and other problems, to achieve the effect of improving the cycle utilization rate, speed and utilization rate.

Pending Publication Date: 2018-04-27
ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the 650-750°C medium-temperature waste heat brought out by coke oven raw gas accounts for 37% of the coke oven heat expenditure. Efficient recovery of this part of heat is particularly important for secondary energy recovery and utilization in coking enterprises, but the composition of coke oven raw gas is extremely complex and extremely complex. Easy to condense and precipitate, adhere to the heat exchange device and cause graphitization effect
At present, rising pipe vaporization cooling devices and HYWHR technology are mainly used to recover the waste heat of coke oven raw gas, but the heat recovery efficiency is low, the product types are single, and water leakage from the rising pipe of the coke oven to the coking chamber of the coke oven is prone to occur, which affects the safe production of the coke oven

Method used

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  • Coke oven raw gas heat continuous recovery system

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Embodiment Construction

[0020] The specific embodiment of the present invention will be further described below in conjunction with accompanying drawing:

[0021] Such as figure 1 As shown, a coke oven raw gas heat recovery system without interruption according to the present invention includes a high-temperature dust collector 2, a waste heat boiler 13, a low-temperature heat exchanger 7, a deaerator 5, a desalinated water tank 3, a heating furnace 16, a Temperature and decompression device 14, steam superheater 15 and decompression device 17; described waste heat boiler 13 is composed of steam drum 20 and steam heat exchanger A 18 connected with steam drum 20 through rising pipe 8 and down pipe 9 respectively, steam exchanger Heater B 19; the raw gas input end of the high temperature dust collector 2 is connected to the gas collecting pipe of the coke oven 1, and the raw gas output end of the high temperature dust collector 2 is connected to the steam heat exchanger A 18 and the steam heat exchange...

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Abstract

The invention relates to a coke oven raw gas heat continuous recovery system. The system comprises a high-temperature dust remover, a waste heat boiler, a low-temperature heat exchanger, a deaerator,a desalting water tank, a heating furnace, a temperature reducing and pressure reducing device, a steam superheater and a pressure reducing device. The waste heat boiler is used for efficiently recovering the heat of coke oven raw gas, multi-parameter steam is produced to be used by high-voltage power generation users and low-pressure steam users, internal steam of a process system is recycled, and the purpose of energy conservation is achieved; meanwhile, continuous operation of the waste heat recovery process system is guaranteed, and safe production of a coke oven is not influenced.

Description

technical field [0001] The invention relates to the technical field of waste heat utilization of coke oven raw gas, in particular to a heat recovery system for coke oven raw gas without interruption. Background technique [0002] The coking process is essentially an industrial process with carbon element flow as the main context, so solving the energy saving and consumption reduction of carbon element flow is of great significance for optimizing the coking process. The heat expenditure in the coke production process is mainly composed of the 950-1050 ℃ high-temperature waste heat brought out by the red coke from the coke oven, the 650-750 ℃ ​​medium-temperature waste heat brought out by the coke oven raw gas, and the 180-250 ℃ coke oven flue gas. ℃ low temperature waste heat and furnace surface heat loss consists of four parts. Among them, the 650-750°C medium-temperature waste heat brought out by coke oven raw gas accounts for 37% of the coke oven heat expenditure. Efficie...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): F22B1/18F22B33/18C10B27/00C10B43/00
CPCF22B1/18F22B33/18C10B27/00C10B43/00Y02P20/129
Inventor 付立欣许桂瑛金基浩李桦蒋富何玉涛肖丽任众李旭东
Owner ACRE COKING & REFRACTORY ENG CONSULTING CORP DALIAN MCC
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