Coal mine methane preheating catalytic oxidation device with multiple reaction chambers

A catalytic oxidizer, multi-reaction chamber technology, applied in chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of large TFRR resistance loss, high maintenance cost, large TFRR footprint, etc., and reduce the volume. And the effect of reducing the floor space, improving operating economy, and reducing maintenance costs

Inactive Publication Date: 2011-10-05
SHANDONG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, from the perspective of practical application, only the thermal countercurrent reaction technology has been successfully applied commercially in the coal mine field.
However, the use of TFRR technology to treat coal mine exhaust gas still has the following problems: (1) TFRR occupies a relatively large area, for example, the TFRR unit of MEGTEC Company needs to process 150m 3 / s gas, the device covers an area of ​​about (63×14.62×4.49) m; (2) The oxidation bed of TFRR is composed of a large number of honeycomb ceramics, and the honeycomb ceramics will crack, break and block after long-term use , Generally speaking, the honeycomb ceramics need to be replaced once a year, and the maintenance cost is too high; (3) The resistance loss of TFRR is very large, generally above 8000KPa, and the energy consumption of the fan is very high; (4) The airflow in the oxidation bed of TFRR needs to be constantly Change the direction to ensure that the high temperature area is maintained in the middle of the oxidation bed, which requires a high degree of automatic control and high operating technology requirements
These main problems increase the difficulty of popularization and application of TFRR technology

Method used

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  • Coal mine methane preheating catalytic oxidation device with multiple reaction chambers
  • Coal mine methane preheating catalytic oxidation device with multiple reaction chambers
  • Coal mine methane preheating catalytic oxidation device with multiple reaction chambers

Examples

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Embodiment 1

[0030] exist Figure 1-4 In the shown embodiment 1: the coal mine exhaust air gas preheating catalytic oxidizer with four reaction chambers 16 includes an exhaust air supply system, a preheater 8, a reaction chamber 16, an intake and exhaust system, and air extraction and heat extraction. systems, measurement and control systems. in:

[0031] The exhaust air supply system includes a fan 1, a first exhaust air conveying pipeline 2 and a second exhaust air conveying pipeline 7, one end of the first exhaust air conveying pipeline 2 is connected with the exhaust exhaust outlet of the mine, and the other end is communicated with the exhaust fan 1 The second exhaust air conveying pipeline 7;

[0032] The preheater 8 includes a preheater core 39, a preheater exhaust air inlet 44, a preheater exhaust air outlet 43, a preheater exhaust gas inlet 42, a preheater exhaust gas outlet 38, a preheater housing 41 and a fourth Insulation layer 40, wherein the preheater core 39 adopts an air...

Embodiment 2

[0038] exist Figure 5-6 In the shown embodiment 2: the coal mine exhaust gas preheating catalytic oxidizer has six reaction chambers 16; Air distribution bellows 25, three waste gas collection boxes 28, three shrink tubes 34, waste gas pipe 36, waste gas flaring pipe 12, the intake pipe 26 is provided with four intake branch pipes 22, and the waste gas pipe 36 is provided with three waste gas branch pipes 35, and the rest are the same as in Example 1.

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Abstract

The invention relates to a coal mine methane preheating catalytic oxidation device with multiple reaction chambers and belongs to technical field of ultralow-concentration methane oxidation. The device comprises a coal mine methane supply system, a pre-heater, even reaction chambers, a suction system, an exhaust system, an exhaust heating system and a measuring and controlling system, wherein an electric heater, a temperature-equalizing and flow-equalizing bed and a catalytic oxidation bed are arranged in each reaction chamber. After starting to heat, the coal mine methane is heated after entering into the pre-heater through the coal mine methane supply system; and then the coal mine methane is supplied to each reaction chamber through the suction system; carbon dioxide and water are oxidized in the catalytic oxidation bed of the reaction chamber; after the reacted heat gas is converged by the exhaust system, one part of the heat gas is used for utilizing the heat; and the residual heat gas enters into the pre-heater and transfers the heat to the fresh coal mine methane, and the residual heat gas is lastly discharged into the atmosphere after being cooled. The coal mine methane preheating catalytic oxidation device with multiple reaction chambers has the advantages of compact structure, low power consumption, simpleness in running, high reliability, and the like.

Description

technical field [0001] The invention relates to a multi-reaction chamber coal mine exhaust air preheating catalytic oxidizer, which belongs to the technical field of ultra-low concentration methane oxidation. Background technique [0002] The main component of coal mine gas is methane, a greenhouse gas whose greenhouse effect is 21 times that of carbon dioxide. In recent years, my country's annual methane emission through coal mine ventilation is more than 15 billion Nm 3 . If this exhaust gas is utilized, it is equivalent to about 23 million tons of standard coal, which can reduce 200 million tons of carbon dioxide equivalent. The concentration of exhaust gas in coal mines is very low, and it is difficult to use traditional burners for direct combustion. The current effective utilization methods are Thermal Flow Reversal Reactor (TFRR for short) and Catalytic Flow Reversal (CFRR for short). . The basic working principle and structure of these two countercurrent oxidatio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/88B01D53/72
Inventor 刘永启刘瑞祥王延遐郑斌高振强
Owner SHANDONG UNIV OF TECH
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