Method and device for separating condensable component liquid drops in gas-phase medium
A gas phase and medium technology, applied in separation methods, combined devices, and dispersed particle separation, can solve problems such as high failure rate, poor treatment effect, and inability to ensure complete condensation, achieving good stability, eliminating supersaturation, good quality effect
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Embodiment 1
[0047] Example 1. Separation of droplets and droplets in flue gas after desulfurization
[0048] A method and device for separating droplets of condensable components in a gas phase medium, used for separating droplets and droplets from flue gas after wet desulfurization. After the flue gas is sprayed, it is wrapped with mist, droplets and trace solid particles, which should be separated to meet the needs of emission reduction. The separation method needs to use a demisting device composed of microporous material 2, and the microporous material 2 is a hollow plate microfiltration membrane, specifically as figure 2 shown.
[0049] The demisting device is set on the top of the closed device 1, the closed device is a desulfurization tower, coupled with the desulfurization tower to form an operating unit, the demisting device is composed of a plurality of microporous materials 2 connected to each other, that is, a hollow plate microfiltration membrane . The hollow plate microf...
Embodiment 2
[0056] Example 2. Recovery of methanol droplets in dimethyl ether scrubbing tail gas
[0057] A method and device for separating condensable component droplets in a gas phase medium, which are used to recover methanol droplets from dimethyl ether scrubbing tail gas. The separation method needs to use a closed device with a built-in microporous material 2, and the microporous material 2 is a tubular ultrafiltration membrane, specifically as image 3 shown.
[0058] In this example, the scrubbing tail gas is produced during the process of producing dimethyl ether by methanol vapor phase dehydration, and the weight ratio of the main components is roughly: 10.6% methanol, 3.5% dimethyl ether, 31% CO, 21.8% CO 2 , 7% hydrogen, 4.3% water and 21.8% CH 4 etc., the temperature is about 40°C, and the gauge pressure is about 1.1MPa. Methanol is a supersaturated condensable component under this working condition, which can be separated and recovered.
[0059] A microporous material 2...
Embodiment 3
[0066] Embodiment 3. Eliminate maleic anhydride supersaturation and acid mist in maleic anhydride synthesis gas
[0067] A method and device for separating condensable component droplets in a gas phase medium, used for eliminating supersaturation and acid mist of maleic anhydride synthesis gas in the production of maleic anhydride. The separation method needs to use a closed device 1 with a built-in microporous material 2, and the microporous material 2 is a tubular microfiltration membrane, specifically as image 3 shown.
[0068] In this embodiment, after cooling and preliminary gas-liquid separation, the maleic anhydride synthesis gas has a temperature of 63-65° C. and a gauge pressure of 0.1-0.12 MPa. It contains a certain amount of maleic anhydride droplets, which need to be separated and recovered.
[0069] The microporous material 2 is arranged in the closed device 1, that is, the tubular microfiltration membrane, and the tubular microfiltration membrane separates the ...
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Abstract
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Application Information
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