Ceramic membrane condensation treatment recycling method for smoke waste heat and water of power plant
A flue gas waste heat and recovery method technology, which is applied in the direction of steam condensation, separation methods, chemical instruments and methods, etc., can solve problems such as dew point corrosion, and achieve the effect of simplifying the process flow and effectively utilizing water resources
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Embodiment 1
[0017] The flue gas with a large amount of water vapor in a power plant with an exhaust gas temperature of 70°C passes through an 8nm single-tube alumina ceramic membrane separation device, and the membrane surface velocity is controlled to be 0.032m·s -1 , the transmembrane pressure difference is 0.45MPa, and the flow rate of circulating water on the permeate side is 2.5L h -1 , to detect the temperature change before and after the flue gas passes through the ceramic membrane, and the change of the water temperature and water quality on the circulation side after the water vapor condenses and passes through the ceramic membrane.
[0018] Among them, the flue gas composition before separation: CO 2 : 11-16%, H 2 O: 5-7%, O 2 : 3-4%, N 2 : 70-75%, CO: ~20ppm, SOx: <800ppm, NOx: 500-800ppm, temperature: 45~120℃. After the separation, the water vapor component in the flue gas is reduced. Since the loss of the remaining water vapor component is less than 4% to 6%, the remainin...
Embodiment 2
[0026] The flue gas with a large amount of water vapor in a power plant with an exhaust gas temperature of 110°C passes through a 5nm single-tube alumina ceramic membrane separation device, and the membrane surface velocity is controlled to be 0.048m·s -1 , the transmembrane pressure difference is 0.4MPa, and the flow rate of circulating water on the permeate side is 2.5L h -1 , to detect the temperature change before and after the flue gas passes through the ceramic membrane, and the change of the water temperature and water quality on the circulation side after the water vapor condenses and passes through the ceramic membrane. The water vapor recovery rate can reach 16%, and the energy recovery rate can reach 12%.
Embodiment 3
[0028] The flue gas with a large amount of water vapor in a power plant with an exhaust gas temperature of 50°C passes through a 12nm single-tube alumina ceramic membrane separation device, and the membrane surface velocity is controlled to be 0.048m·s -1 , the transmembrane pressure difference is 0.2MPa, and the flow rate of circulating water on the permeate side is 25L h -1 , to detect the temperature change before and after the flue gas passes through the ceramic membrane, and the change of the water temperature and water quality on the circulation side after the water vapor condenses and passes through the ceramic membrane. The water vapor recovery rate reaches 10%, and the energy recovery rate is lower than the detection limit of 5%.
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