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Double-layer hot air distribution pipe

A hot air distribution, double-layer technology, applied in the direction of pipes, branch pipelines, pipes/pipe joints/fittings, etc., can solve the problems of low temperature on both sides, uneven temperature distribution, high central temperature, and improve the difference in hot air quality , The effect of solving uneven temperature distribution and reducing the temperature difference of hot air

Active Publication Date: 2020-05-12
SHANDONG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This heating start technology has the advantages of simple structure, easy control, etc., but there are also many disadvantages: for example, after the electric heater stops heating, it is easy to oxidize and become brittle in the high temperature zone of the oxidizing atmosphere for a long time, or even break, and lose the function of restarting.
But there are problems: (1) The temperature distribution on the same cross-section of the oxidation bed is not uniform, the central temperature is high, the temperature on both sides is low, the front side temperature is high, and the rear side temperature is low, which affects the establishment of the entire temperature field of the oxidation bed and the maintenance of the device. The oxidation rate will have a great impact; for the drying space of the drying device, there is also the problem of uneven temperature distribution. The bigger the space, the worse the drying effect
(2) For a larger heating space, due to the longer heat distribution pipeline, the overall thermal deformation is more obvious
[0007] The reason is that in the process of hot air distribution, along with the outward heat dissipation of the pipe wall, whether along the main pipe or along the branch pipes, the temperature of the hot air gradually decreases from front to back. The key factor of temperature unevenness, and the effect of simple structural adjustment is not obvious, and the essential problem cannot be solved

Method used

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Examples

Experimental program
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Effect test

Embodiment 1

[0046] like Figure 1~5 As shown: in this embodiment, the main pipe 1 is provided with three sections connected head to tail along the axial direction, and the left end of each section of the main pipe 1 is the air inlet end, and the right end is the air outlet end. 2. Three branch pipes 3 are evenly distributed on the upper and lower sides of each section of the main pipe 1. The branch pipes 3 are arranged along the radial direction of the main pipe 1. The right end of the main pipe end pipe 2 is closed, and the upper and lower sides of the main pipe end pipe 2 are also symmetrically arranged. Three branch pipes 3. The end of each branch pipe 3 close to the main pipe 1 or the end pipe 2 of the main pipe is the air inlet end, and the end of each branch pipe 3 far away from the main pipe 1 or away from the main pipe end pipe 2 is the gas outlet end, and each branch pipe 3 is provided with a head-to-tail connection in the axial direction In the two sections, the gas outlet end ...

Embodiment 2

[0058] like Figure 6~7 As shown: the difference between embodiment 2 and embodiment 1 is that the delivery main pipe docking cover 601 of the main delivery main pipe 6 is spaced apart from the inner wall of the corresponding distribution main pipe 5 of this section, that is, both ends of the main pipe distribution chamber 8 are open. The delivery branch pipe docking cover 1001 of the delivery branch pipe 10 is spaced apart from the inner wall of the corresponding distribution branch pipe 9 , that is, both ends of the distribution chamber 11 of the branch pipe are open. Ensure that the hot air flow is more stable.

Embodiment 3

[0060] like Figure 8~12 As shown: the difference between embodiment 3 and embodiment 1 is that a pre-allocation main pipe 16 is arranged between the distribution main pipe 5 and the conveying main pipe 6 of each section of main pipe 1, and the pre-allocation main pipe 16 and the corresponding distribution main pipe 5 and the conveying main pipe 6 They are evenly spaced, so that a main pipe distribution cavity 8 is formed between the pre-distribution main pipe 16 and the distribution main pipe 5, and a main pipe pre-distribution chamber 18 is formed between the delivery main pipe 6 and the pre-distribution main pipe 16. The intake end of the conveying main pipe 6 is arranged within the intake end of the pre-distribution main pipe 16, thereby forming a gap for connecting the pre-distribution main pipe 16 intake end and the conveying main pipe 6 intake end at the pre-distribution main pipe 16 intake end. The main pipe communicates with the chamber 17.

[0061] The two sides bet...

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Abstract

A double-layer hot air distribution pipe belongs to the technical field of ultra-low concentration methane thermal countercurrent oxidation and low-density energy recovery. It is characterized in that it includes a main pipe (1) and a plurality of branch pipes (3) arranged on both sides of the main pipe (1), and the outlet end of the main pipe (1) is provided with a main pipe end pipe (2); each section of the main pipe (1) includes The conveying main pipe (6) and the distributing main pipe (5) are arranged sequentially from the inside to the outside, and the gas outlet end of the conveying main pipe (6) is simultaneously connected with the main pipe distributing cavity (8) and the conveying main pipe (6) of the next main pipe (1); Each branch pipe (3) includes a delivery branch pipe (10) and a distribution branch pipe (9) arranged sequentially from the inside to the outside, and the gas outlet end of the delivery branch pipe (10) is connected with the delivery branch pipe (10) and The distribution branch pipe (9) is connected. The double-layer hot air distribution pipe fundamentally solves the problem of uneven temperature distribution, making the temperature distribution of the oxidation bed more uniform on the same cross section.

Description

technical field [0001] A double-layer hot air distribution pipe belongs to the technical field of ultra-low concentration methane thermal countercurrent oxidation and low-density energy recovery. Background technique [0002] The main component of coal mine gas is methane, which is both a gas energy source and a greenhouse gas. In addition to partial extraction, most of the gas is directly discharged into the atmosphere through the coal mine ventilation system, causing energy waste and air pollution. Thermal flow-reversal reactor (TFRR for short) in coal mine exhaust air can oxidize methane in exhaust air into carbon dioxide and water, realizing the utilization of low-quality energy and reducing greenhouse gas emissions. [0003] Before the coal mine exhaust air gas oxidation device is in normal operation, it needs to use a certain amount of energy to heat the central part of the oxidation bed to about 900~1000°C, and form a certain temperature distribution, which will dire...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F16L41/02
CPCF16L41/021
Inventor 尤彦彦刘永启高振强刘瑞祥毛明明
Owner SHANDONG UNIV OF TECH
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