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Method for increasing concentration of gas easy to adsorb by using pressure swing adsorption method

A pressure swing adsorption method, an easy-to-adsorb technology, applied in separation methods, chemical instruments and methods, dispersed particle separation, etc., can solve the problems of unfavorable methane concentration, reduced product recovery rate, high replacement gas pressure, etc., to improve the treatment rate. , The effect of reducing the loss of recovery rate and increasing the proportion

Active Publication Date: 2019-10-22
盖氏科技 +1
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AI Technical Summary

Problems solved by technology

[0003] At present, the process of gas adsorption separation generally includes the steps of adsorption, pressure equalization, desorption, and final filling. Replacement is also one of the commonly used operations in the adsorption process, which can be used to increase the product concentration to a certain extent. In addition to the impurity gas, the gas in the tower also has part of the product gas. The direct discharge of the replaced gas will cause the loss of the target product gas, reduce the product recovery rate and cause pollution at the same time. If the replaced gas is sent back to the raw material tank, will reduce the gas handling capacity of the adsorbent
In addition, when gas separation is carried out under high pressure conditions, low-pressure replacement is generally used. Low-pressure replacement operation not only has a limited effect on the enrichment of product gas, but also causes gas desorption due to the reduction of the partial pressure of the target gas, which reduces the treatment efficiency of the target gas. Amount and thickening effect
[0004] CN 107694284A discloses a multi-tower replacement vacuum pressure swing adsorption method for concentrating gas layer methane, mainly including pressurization, CH 4 Adsorption, CO 2 Substitution, pressure reduction, adsorbent vacuum desorption, vacuum purging and other steps, this method does not use pressure equalization operation before the replacement, the pressure of the replacement gas is relatively high, which will not only replace the unadsorbed gas in the tower, but also replace methane, resulting in gas The separation effect is not good, and the use of CO 2 The replacement will also introduce other impurity gases, which is not conducive to the enrichment of methane in coalbed methane
CN102350171A discloses a gas separation method using a replacement method. There are at least 6 adsorption towers combined together to realize cyclic adsorption. Each adsorption tower completes the processes of adsorption, depressurization, emptying, replacement, vacuuming, boosting and charging in sequence. Circulation process, at the same time, each adsorption tower completes a process, but this method is to absorb the impurity gas in the raw material gas, and complete the follow-up process on this basis, the focus is on gas separation, for the adsorption and enrichment of product gas The operating procedures and the coordination of each adsorption tower will be quite different

Method used

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  • Method for increasing concentration of gas easy to adsorb by using pressure swing adsorption method
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  • Method for increasing concentration of gas easy to adsorb by using pressure swing adsorption method

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Embodiment 1

[0070] This embodiment provides a method for enriching methane by pressure swing adsorption. The method is operated by a device consisting of five adsorption towers arranged in parallel. The structural connection diagram of the device is as follows figure 1 As shown, it includes the first adsorption tower 101A, the second adsorption tower 101B, the third adsorption tower 101C, the fourth adsorption tower 101D and the fifth adsorption tower 101E, and also includes a feed line, a pressure equalization line, a replacement line, a desorption line, The final filling line, each pipeline is independently connected to 5 adsorption towers, and all of them are equipped with valves; the replacement line and the desorption line are connected to the product gas storage device 201.

[0071] This embodiment takes the operation process of 5 towers as an example to specifically illustrate the operation process of enriching methane; wherein the adsorption pressure used is 120kPa, and the desorpt...

Embodiment 2

[0090] This embodiment provides a method for enriching methane by pressure swing adsorption. The method is operated by a device consisting of five adsorption towers arranged in parallel. The structural connection diagram of the device is as follows image 3 As shown, the overall structure and connection relationship are basically the same as in Example 1, the difference is that the operating pipeline includes a decompression line in addition to a feed line, a pressure equalization line, a replacement line, a desorption line, and a final filling line.

[0091] This embodiment takes the operation process of 5 towers as an example to specifically illustrate the operation process of enriching methane; wherein the adsorption pressure used is 550kPa, and the desorption pressure is 25kPa. Taking the first adsorption tower 101A as an example, it includes 18 steps of operation process, which are respectively : 1. Adsorption; 2. Adsorption; 3. Adsorption, 4. Adsorption; 5. Empty; 6. Equa...

Embodiment 3

[0110] This embodiment provides a method for enriching methane by the pressure swing adsorption method. The method is operated by a device composed of five adsorption towers arranged in parallel. The overall structure and connection relationship are basically consistent with those of Embodiment 1, the difference is that: In addition to the feed line, pressure equalization line, replacement line, desorption line, and final filling line, the operating pipeline also includes a decompression line.

[0111] In this embodiment, the operation flow of 5 towers is taken as an example, and the operation procedure for enriching methane is the same as that in Embodiment 2.

[0112] Taking the first adsorption tower 101A as an example, the 20-step operation process will be described in detail below:

[0113] 1-4. Adsorption: Open the valves 101A and 102A, the raw material gas enters the first adsorption tower 101A, and contacts with the adsorbent, the adsorption pressure is 950kPa, in whic...

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Abstract

The invention provides a method for increasing the concentration of a gas easy to adsorb by using a pressure swing adsorption method. The method comprises the following steps: (1) feeding a raw material gas into a first adsorption tower, and performing adsorption operation till an adsorbent is saturated; (2) performing pressure equalizing operation on a first adsorption tower after adsorption; (3)introducing a product gas into an unadsorbed gas for exchange, and blowing an exchanged gas into other adsorption towers; (4) performing pressure equalizing operation on the first adsorption tower after exchange for a second time; (5) performing vacuum desorption on the first adsorption tower so as to obtain a product gas; (6) pressurizing the first adsorption tower after desorption. Through theprocedures, multiple adsorption towers cooperate to achieve concentration increase of the gas easy to adsorb, particularly the product gas is adopted as an exchange gas, the exchanged gas is fed intoother adsorption towers, and pressure equalizing operation is implemented after exchange, so that not only is the exchange effect improved, but also the concentration and the recycling rate of a component easy to adsorb can be increased.

Description

technical field [0001] The invention belongs to the technical field of gas adsorption, and relates to a method for enriching easily adsorbed gas by a pressure swing adsorption method, in particular to a method for enriching an easily adsorbed gas by a pressure swing adsorption method including product gas replacement. Background technique [0002] Pressure swing adsorption is a commonly used gas separation method in the chemical industry. It has been widely used in industry due to its advantages such as strong flexibility, low operating cost and good separation effect. According to the need, after adsorption and separation, the easily adsorbed gas can be recovered, and the remaining gas that is difficult to adsorb can also be recovered, or both can be recovered at the same time. Among them, the adsorbent is one of the factors affecting the separation effect, and the design optimization of the adsorption process is also crucial to the improvement of the separation effect. ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/047
CPCB01D53/047
Inventor 胡国平李刚肖月竹保罗·安东尼·韦伯利米切·曼宁
Owner 盖氏科技
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