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Multi-tower pressure swing adsorption grading flushing device and method

A pressure swing adsorption and flushing device technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve the problems of poor regeneration effect and short flushing time, and achieve good regeneration effect, long regeneration time, and control The effect of impurity content

Inactive Publication Date: 2017-12-26
CHENGDU JUTAO OIL ENG CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] For the regeneration of the adsorbent in the pressure swing adsorption process, the tower-to-tower flushing method was adopted in the early stage. The disadvantages of this regeneration method are: a. High pressure first and then low pressure, resulting in high-purity gas flushing first and then low-purity gas flushing, and the regeneration effect is not good; b. , short flushing time
[0003] However, when the product gas purity is high (such as hydrogen purity ≥ 99.99%) or the impurity is strict (such as CO+CO 2 ≤20PPm), the defects of this regeneration method are highlighted: a. The flushing gas is preferably low-purity gas in the early stage, and high-purity gas for regeneration in the later stage; b. The regeneration time is prolonged and the regeneration is cleaner

Method used

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  • Multi-tower pressure swing adsorption grading flushing device and method
  • Multi-tower pressure swing adsorption grading flushing device and method
  • Multi-tower pressure swing adsorption grading flushing device and method

Examples

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Embodiment 1

[0043] Such as figure 1 As shown, the multi-tower pressure swing adsorption grading flushing device in this embodiment includes eight adsorption towers, respectively numbered T201A, T201B, T201C, T201D, T201E, T201F, T201G and T201H.

[0044] The raw material gas end of each adsorption tower is connected with the raw material gas input pipe and the desorbed gas output pipe, the inlet of the raw gas input pipe is connected with the outlet of the raw material gas buffer tank, and the inlet of the raw material gas buffer tank is connected with the raw material gas source.

[0045] The product end of each adsorption tower is connected to the product gas output pipe, and each adsorption tower is connected to the parallel discharge circuit and the flushing circuit, and the parallel discharge circuit is respectively connected to the inlet of the high-pressure parallel discharge tank (V202A) and the inlet of the low-pressure parallel discharge tank (V202B) The flushing circuit is resp...

Embodiment 2

[0071] Such as image 3 As shown, the multi-tower pressure swing adsorption classification flushing device of this embodiment includes fourteen adsorption towers, respectively numbered as T101A, T101B, T101C, T101D, T101E, T101F, T101G, T101H, T101I, T101J, T101K, T101L, T101M, and T101N.

[0072] The raw gas end of each adsorption tower is connected to the raw gas input pipe and the desorbed gas output pipe, the inlet of the raw gas input pipe is connected to the outlet of the decarburization buffer tank, and the inlet of the decarburization buffer tank is respectively connected to the raw gas source and the helium source connected.

[0073] The product end of each adsorption tower is connected to the product gas output pipe, and each adsorption tower is connected to the parallel discharge circuit and the flushing circuit, and the parallel discharge circuit is respectively connected to the inlet of the high-pressure parallel discharge tank (V102A) and the inlet of the low-pr...

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Abstract

The invention discloses a multi-tower pressure swing adsorption grading flushing device and a method. Two concurrent discharge vessels are connected with an adsorption tower; one vessel is a high-pressure concurrent discharge vessel for storing product gas in higher purity and the other vessel is a low-pressure concurrent discharge vessel for storing product gas in lower purity; adjusting valves for adjusting the flushing flux are arranged at an outlet of the high-pressure concurrent discharge vessel and at the outlet of the low-pressure concurrent discharge vessel; the product gas in lower purity in the low-pressure concurrent discharge vessel is firstly used for flushing and then the product gas in higher purity in the high-pressure concurrent discharge vessel is used for later flushing in the flushing process; the flushing time is adjusted according to the pressure of the high-pressure concurrent discharge vessel and the low-pressure concurrent discharge vessel, so that the complete gas exhausting in the flushing process is guaranteed; the practical running regenerating effect is excellent; and the impurity content in the product gas can be effectively controlled.

Description

technical field [0001] The invention belongs to the technical field of pressure swing adsorption technology, and in particular relates to a multi-tower pressure swing adsorption classification flushing device and method. Background technique [0002] For the regeneration of the adsorbent in the pressure swing adsorption process, the tower-to-tower flushing method was adopted in the early stage. The disadvantages of this regeneration method are: a. High pressure first and then low pressure, resulting in high-purity gas flushing first and then low-purity gas flushing, and the regeneration effect is not good; b. , The washing time is short. After improvement, the parallel release tank process is now commonly used. The improvement of this regeneration method is: put the forward release gas into the forward release tank, and the forward release tank will flush the adsorption tower. The advantages of this regeneration process are: a. The gas is mixed in the tank in the tank, and ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/047B01D53/053
CPCB01D53/047B01D53/053B01D2259/40003B01D2259/40007B01D2259/40045B01D2259/40052B01D2259/406
Inventor 温岚丁波曾启明刘毅
Owner CHENGDU JUTAO OIL ENG CO LTD
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