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Method for trapping CO2 by using double tube micro-reactor

A micro-reactor and reactor technology, applied in the field of CO2 capture, can solve the problems of limited treatment capacity, unsuitable for large treatment capacity, etc., and achieve the effects of large treatment capacity, reduced CO2 absorption cost, and safe operation.

Active Publication Date: 2011-04-20
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

There is a kind of microchannel reactor reported in the literature, which is a tubular single channel structure (Y type or T type single channel microreactor), which can be used for liquid-liquid or gas-liquid mass transfer process, but the gas of this kind of reactor -The liquid mass transfer enhancement process is only realized by using micronized reactor size, which is suitable for CO 2 There is still room for improvement in the enhancement of mass transfer processes controlled by trapping such liquid films
Moreover, the single microchannel structure also limits the processing capacity, which is not suitable for large-capacity industrial mass transfer processes, such as CO in industrial tail gas. 2 Discharge treatment

Method used

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  • Method for trapping CO2 by using double tube micro-reactor
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  • Method for trapping CO2 by using double tube micro-reactor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Embodiment 1: the casing type microreactor structure that adopts is as figure 1 As shown, the radial spacing of the annular microchannel is 250 μm, the diameter of the micropore is 10 μm, the length of the micropore part is 17.0 mm, and the length of the microchannel is 156.0 mm. Experimental device such as Figure 4 As shown, the N 2 with CO 2 The mixed gas (of which CO 2 content of 90%) through the gas flow meter 7, enter the inner pipe 5 from the gas inlet 1 horizontal direction at one end of the microreactor, and the pressure of the gas inlet is measured by the pressure gauge; the absorption liquid is then passed through the peristaltic pump 10, The liquid flow meter 9 is injected into the outer pipe 6 of the sleeve type microreactor from the liquid inlet 2 on the side of the microreactor 8, and the gas-liquid two-phase impacts cross-flow contact in the micropore part of the microreactor, and is in the entire annular microchannel The mass transfer process is com...

Embodiment 2

[0031] Embodiment 2: the casing microreactor and technological process that adopt are identical with embodiment 1.

[0032] Weigh 400 g of NaOH, dissolve it in deionized water to prepare 10 L of NaOH solution with a concentration of 3.8% by mass, and place it in a storage tank to seal it. The size of the sleeve-type microreactor used in this experiment is: the diameter of the micropore is 10 μm, the radial spacing of the annular microchannel is 500 μm, the length of the micropore part is 17.0 mm, and the length of the microchannel is 156.0 mm. During the experiment, the N 2 with CO 2 The mixed gas (of which CO 2 The content is 85%) through the gas flow meter into the inner tube of the horizontal sleeve type microreactor; the liquid in the liquid storage tank is injected into the outer tube of the microreactor by the peristaltic pump connected in series. The gas-liquid two-phase impact contacts in the micropore part of the microreactor, and the entire mass transfer process i...

Embodiment 3-5

[0033] Embodiment 3-5: the jacketed microreactor and technological process that adopt are identical with example 1.

[0034] Prepare the absorbent in the reservoir and seal it. During the experiment, the N 2 with CO 2 The mixed gas (of which CO 2 The content is shown in Table 1) through the gas flowmeter into the inner tube of the casing microreactor placed horizontally; the liquid in the liquid storage tank is injected into the outer tube of the microreactor by the peristaltic pump connected in series. The length of the micropore part of the sleeve-type microreactor used in the experiment is 17.0mm, and the length of the microchannel is 156.0mm. Other dimensions are shown in Table 1. The gas-liquid two-phase impact contacts in the micropore part of the microreactor, and completes the entire mass transfer process in the microchannel part. In the experiment, glass thermometers were used to measure the temperature of gas, liquid and gas-liquid phase separation bottle respect...

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Abstract

The invention relates to a method for trapping carbon dioxide (CO2) by using a double tube micro-reactor. The method comprises the following steps of: introducing CO2-containing mixed gas into an inner tube of the micro-reactor, wherein the pressure intensity at a gas inlet is 0.1 to 5MPa and the gas-phase linear velocity is 1.0 to 20.0m / s; injecting absorption liquid into an outer tube of the micro-reactor and keeping liquid-phase linear velocity within a range of between 0.01 and 1m / s to form a stable annular liquid membrane; allowing the gas to burst out from a micro-channel of the inner tube, dispersing the gas phase into micron-scale small bubbles and allowing the small bubble to collide the liquid membrane which has micron-scale thickness and is formed in the outer tube on a microporous part of the micro-reactor by cross flow; and allowing the gas and the liquid to flow into the annular micro-channel of the micro-reactor in parallel to finish a micro mass transfer absorption process. The method can greatly enhance the gas-liquid mass transfer process of which the reaction is controlled by the liquid membrane, and obviously improve the CO2 absorption rate; and the processing load is increased by scores of times compared with that of a single-channel micro-reactor. The method has a simple process and is low in cost.

Description

Technical field: [0001] The present invention relates to the capture of CO 2 method, especially a method for capturing CO using a jacketed microreactor 2 Methods. It can be used for gas purification and greenhouse gas emission reduction. Background technique: [0002] carbon dioxide (CO 2 ) emissions are the main cause of the greenhouse effect, so CO 2 Emission reduction and resource utilization have become the focus of energy conservation and emission reduction in countries all over the world. CO 2 The capture of CO is a prerequisite for its utilization and burial, while the low-cost CO 2 It is quite difficult to capture large quantities. Absorb CO 2 There are many methods, but no matter what method is used to decarbonize, the mass transfer efficiency of the decarbonization process directly affects the CO 2 Circulation of absorption liquid and CO in purified gas 2 content, which also affects the cost of decarbonization. The absorption rate of decarbonization is h...

Claims

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Application Information

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IPC IPC(8): B01D53/18B01D53/62B01J19/00B01J10/00C01B31/20C01B32/50
CPCY02C10/04Y02A50/20Y02C20/40Y02P20/151
Inventor 陈建峰陈桂子王洁欣邵磊李鹏飞
Owner BEIJING UNIV OF CHEM TECH
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