Coal chemical industry solid waste drying tail gas treatment device and treatment method

A technology of coal chemical industry and exhaust gas, which is applied in the direction of chemical instruments and methods, combined devices, gas treatment, etc., can solve the problems of high loss on ignition, difficult solid waste treatment, unsuitable concrete, etc., and achieves low environmental impact rate and low resource consumption. The effect of high utilization rate and stable operation

Pending Publication Date: 2020-03-31
HENAN XINLIANXIN FERTILIZER
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The new entrained entrained gasification technology has become the mainstream process in the coal chemical industry. The entrained entrained bed process has a high carbon conversion rate, and the waste water generated can be directly treated in daily life. However, the solid waste generated by it is difficult to deal with, mainly due to gasification coarse residue and gasification filter cake. (Fine slag) The resource utilization rate is not high; with the development of technology, scholars have realized that the components of gasification ash slag are CaO, SiO 2 The composition is high, but it contains a certain amount of residual carbon at the same time, resulting in a high loss on ignition, so it is not suitable for use as the main material of concrete; but after the experimental proportioning, it can be used as an auxiliary material in the range of 5-13% to enter the cement Or commercial mixing stations; with the development of the national economy, real estate and high-speed rail construction, a large amount of cement needs to be used. According to the statistics of the association, my country's cement production capacity is about 2.7 billion tons, and the annual output of coal chemical solid waste is about 200 million tons. At present, the mainstream ash treatment idea is landfill, and a large amount of coal chemical ash solid waste has accumulated into a huge slag field. Therefore, it is a promising market to turn coal chemical ash into cement materials, and it has far-reaching environmental protection. and economic benefits
However, due to the high moisture content of gasification ash, which is 25%-50% on average, the ash must be dehydrated in the early stage of utilization. The conventional and feasible process route is mechanical pressing + drying with a dryer. After accounting, the process can be improved by 10% The rate of return has become the mainstream process for some enterprises to deal with ash solid waste. However, whether it is dried by hot air or steam dryer, for gasified ash, the residual moisture in the ash contains 100% COD. -300mg / L, ammonia nitrogen is 100-250mg / L, and the length of the white feather tail is 70-80m when discharged; the above-mentioned white smoke and volatile odor cannot meet the requirements of environmental protection testing

Method used

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  • Coal chemical industry solid waste drying tail gas treatment device and treatment method

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Effect test

Embodiment 1

[0046] A coal chemical solid waste drying tail gas treatment device, including a dryer 1, a dry ash discharge device 2 is installed at the end of the dryer 1, and the bottom of the dry ash discharge device 2 is connected to the finished product through a dry ash conveying device 3 The gas outlet at the top of the dry ash discharge device 2 is connected to the odor absorption tower 6 through the dust removal unit, and the gas phase outlet of the odor absorption tower 6 is connected to the flue gas condensate collector through the tube side of the gas-gas heat exchanger 10 13 connected, the gas phase outlet of the flue gas condensate collector 13 is connected with the outer cylinder of the telescopic chimney 15; The tuyeres are connected, and the second tee 20 and the system induced draft fan 14 are arranged in turn between the gas phase outlet of the flue gas condensate collector 13 and the outer cylinder of the sleeve chimney 15, and the shell side outlet of the gas-gas heat ex...

Embodiment 2

[0062] A coal chemical solid waste drying tail gas treatment device, including a dryer 1, a dry ash discharge device 2 is installed at the end of the dryer 1, and the bottom of the dry ash discharge device 2 is connected to the finished product through a dry ash conveying device 3 The gas outlet at the top of the dry ash discharge device 2 is connected to the odor absorption tower 6 through the dust removal unit, and the gas phase outlet of the odor absorption tower 6 is connected to the flue gas condensate collector through the tube side of the gas-gas heat exchanger 10 13 connected, the gas phase outlet of the flue gas condensate collector 13 is connected with the outer cylinder of the telescopic chimney 15; The tuyeres are connected, and the second tee 20 and the system induced draft fan 14 are arranged in turn between the gas phase outlet of the flue gas condensate collector 13 and the outer cylinder of the sleeve chimney 15, and the shell side outlet of the gas-gas heat ex...

Embodiment 3

[0078]A coal chemical solid waste drying tail gas treatment device, including a dryer 1, a dry ash discharge device 2 is installed at the end of the dryer 1, and the bottom of the dry ash discharge device 2 is connected to the finished product through a dry ash conveying device 3 The gas outlet at the top of the dry ash discharge device 2 is connected to the odor absorption tower 6 through the dust removal unit, and the gas phase outlet of the odor absorption tower 6 is connected to the flue gas condensate collector through the tube side of the gas-gas heat exchanger 10 13 connected, the gas phase outlet of the flue gas condensate collector 13 is connected with the outer cylinder of the telescopic chimney 15; The tuyeres are connected, and the second tee 20 and the system induced draft fan 14 are arranged in turn between the gas phase outlet of the flue gas condensate collector 13 and the outer cylinder of the sleeve chimney 15, and the shell side outlet of the gas-gas heat exc...

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Abstract

The invention belongs to a coal chemical industry solid waste drying tail gas treatment device and treatment method. The device comprises a drying machine, a dry ash discharging device is arranged atthe tail end of the drying machine, the bottom of the dry ash discharging device is connected to a finished product warehouse through a dry ash conveying device, a gas outlet in the top of the dry ashdischarging device is connected to a peculiar smell absorption tower through a dust removal unit, a gas phase outlet of the peculiar smell absorption tower is connected to a flue gas condensate collector through a gas-gas heat exchanger tube, a gas phase outlet of the flue gas condensate collector is connected to an outer cylinder of a sleeve type chimney, a shell pass inlet of the gas-gas heat exchanger is connected to an air outlet of a system air cooler through a first tee joint, and a second tee joint and a system induced draft fan are arranged between a gas phase outlet of the flue gas condensate collector and the outer cylinder of the sleeve type chimney. The system has the advantages of energy conservation, environmental protection, high resource utilization rate, low environmentalinfluence rate, stable operation, low cost and capability of realizing white smoke removal of tail gas.

Description

technical field [0001] The invention belongs to the technical field of chemical solid waste treatment, and in particular relates to a coal chemical solid waste drying tail gas treatment device and treatment method. Background technique [0002] The new entrained entrained gasification technology has become the mainstream process in the coal chemical industry. The entrained entrained bed process has a high carbon conversion rate, and the waste water generated can be directly treated in daily life. However, the solid waste generated by it is difficult to deal with, mainly due to gasification coarse residue and gasification filter cake. (Fine slag) The resource utilization rate is not high; with the development of technology, scholars have realized that the components of gasification ash slag are CaO, SiO 2 The composition is high, but it contains a certain amount of residual carbon at the same time, resulting in a high loss on ignition, so it is not suitable for use as the mai...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D50/00B01D53/18B01D53/26F28D7/00
CPCB01D53/18B01D53/265F28D7/00B01D2257/406B01D2257/80B01D50/20
Inventor 张庆金曹真真李红明万银霞刘照钊孔垂震孙玉龙宋仁委
Owner HENAN XINLIANXIN FERTILIZER
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