Activated charcoal gas cleaning method and device thereof

A gas purification device and activated coke technology, which is applied in chemical instruments and methods, separation methods, and other chemical processes, can solve the problems of low desulfurization efficiency, no adsorption, and high convective adsorption efficiency, and achieve high space utilization and adsorption efficiency. The effect of improving and saving floor space

Active Publication Date: 2008-11-26
BEIJING SPC ENVIRONMENT PROTECTION TECH
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Disadvantages: The flue gas enters the activated coke bed from the side, the activated coke near the flue gas inlet first undergoes adsorption reaction and reaches saturation first, the flue gas moves from left to right, the adsorption saturation of activated coke decreases in turn, the overall distribution The adsorption saturation of activated coke decreases from left to right, and increases from top to bottom. The adsorption of activated coke on the side near the flue gas outlet is less, so that some of the activated coke discharged is not fully adsorbed. In this way, part of the fresh active coke is discharged and sent for regeneration, so that the circulation of active coke is increased, and the increase of circulation also increases the power consumption and damage, and the amount of regeneration gas increases, resulting in Energy is wasted. In addition, due to the large saturation of the activated coke in the lower part, the desulfurizat

Method used

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  • Activated charcoal gas cleaning method and device thereof
  • Activated charcoal gas cleaning method and device thereof
  • Activated charcoal gas cleaning method and device thereof

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Experimental program
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Effect test

Embodiment 2

[0071] As shown in Figure 9, the difference between this embodiment and the first embodiment is that the feed structure is set as follows: a unit feed port 1 is provided above the unit activated coke bed 2, and the unit feed port 1 passes through the unit The feed port channel 17 is connected with a main feed channel 21, and the main feed channel 21 is connected with the storage bin 8 located below the main feed port 16.

Embodiment 3

[0073] As shown in Figure 10, the difference between this embodiment and the first embodiment is that the discharging structure is set as follows: a unit discharging port 1 is provided below the unit activated coke bed 2, and multiple unit discharging ports 1 It can be divided into several groups. Each group of unit outlet 1 is connected to the primary outlet channel 22 through the unit outlet channel 18, and the above-mentioned multiple primary outlet channels 22 are connected to the main outlet through the secondary outlet channel 23. The material port 20 is connected. According to the number of unit activated coke beds, a three-stage discharge channel or a discharge channel with more than three stages can also be arranged between the secondary discharge channel 23 and the total discharge port 20.

[0074]In each embodiment of the present invention, each unit activated coke bed is provided with an independent feed port and a discharge port to ensure the absorption efficiency of ...

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Abstract

The invention provides an active coke gas purifying method and a device thereof with high desulfurization and denitrification efficiency, energy conservation, little resistance of a bed layer, high utilization rate of the space in an absorption tower and low construction cost. The device comprises a main feed inlet and a gas main outlet which are arranged at the upper part of the absorption tower, a main discharge outlet and a gas main inlet which are arranged at the lower part of the absorption tower and an active coke bed layer which is positioned in the absorption tower, and the active coke bed layer is tilted and has an included angle Alpha with the vertical line. The method has the following steps: gas enters the active code bed layer from the gas main inlet, gas in the tilted bed layer is flowed to the top from the bottom; active coke simultaneously enters the active coke bed layer from the main feed inlet, the active coke in the tilted bed layer is flowed to the bottom from the top; the gas is exhausted from the gas main outlet after the fully tilted convection contact is formed between the gas and the active coke, and the active coke after the saturation by absorption can be discharged from the main discharge outlet.

Description

Technical field [0001] The invention relates to a method and device for purifying activated coke gas. Background technique [0002] Activated coke dry desulfurization and denitrification technology are often used in the purification of flue gas from industrial coal-fired boilers, and also in the purification of gas in absorption towers in the fields of chemical industry, metallurgy, glass, and pharmaceuticals. [0003] <Development of activated coke desulfurization technology> [0004] Activated coke desulfurization technology is a dry desulfurization and denitration technology developed in the 1960s and based on the principle of physical-chemical adsorption. It has the advantages of large adsorption capacity, fast adsorption process and fast catalytic conversion. The activated coke that has adsorbed sulfur dioxide can be reused after regeneration. The regenerated sulfur dioxide can also be made into by-products such as sulfuric acid, liquid sulfur dioxide or elemental sulf...

Claims

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Application Information

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IPC IPC(8): B01D53/04B01J20/20
Inventor 张开元
Owner BEIJING SPC ENVIRONMENT PROTECTION TECH
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