Process method for absorbing sulfur dioxide in flue gas by using aqueous carboxylate solution and regenerating absorbent at same temperature
A technology of sulfur dioxide and process methods, applied in chemical instruments and methods, separation methods, gas treatment, etc., can solve the problems of increasing greenhouse gas carbon dioxide emissions, failing to realize the utilization of sulfur resources, and high cost of ionic liquids, so as to avoid regeneration energy consumption High, avoid equipment corrosion, low price effect
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Embodiment 1
[0024] Take by weighing 10.0g mass concentration and be that the sodium lactate aqueous solution of 51wt% is placed in test tube (1# test tube), this test tube is placed in the water bath of temperature 25 ℃ (that is, absorption temperature is 25 ℃); Take by weighing 10.0g water and place in another In a test tube (2# test tube), the test tube is also placed in a water bath with a temperature of 25°C; the simulated flue gas (mixed gas of nitrogen and sulfur dioxide) with a sulfur dioxide concentration of 1970ppm (volume fraction) is first bubbled through 2# The water in the test tube is then bubbled through the absorbent in the 1# test tube to absorb sulfur dioxide. The flow rate of the simulated flue gas is 100mL / min. The reason for using 2 test tubes is that the simulated flue gas first bubbles through the water in the 2# test tube and absorbs water to reach saturation; in this way, when the sulfur dioxide is absorbed through the 1# test tube, the water content remains unchan...
Embodiment 2
[0027]Take by weighing 10.0g mass concentration and be that the sodium lactate aqueous solution of 51wt% is placed in test tube (1# test tube), this test tube is placed in the water bath of temperature 30 ℃ (that is, absorption temperature is 30 ℃); Take 10.0g water and place in another In a test tube (2# test tube), the test tube is also placed in a water bath with a temperature of 30°C; the simulated flue gas (mixed gas of nitrogen and sulfur dioxide) with a sulfur dioxide concentration of 1970ppm (volume fraction) is first bubbled through 2# The water in the test tube is bubbled through the absorbent of 1# test tube, and the flow rate of simulated flue gas is 100mL / min to absorb sulfur dioxide. After the absorption is saturated, adopt the iodometric method to measure the content of sulfur dioxide in the absorption liquid (see Example 1 for the measurement method); the measurement result shows that the absorption of sulfur dioxide in the absorbent is 0.0551g / g absorbent.
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Embodiment 3
[0030] Take by weighing 10.0g mass concentration and be that the sodium lactate aqueous solution of 51wt% is placed in test tube (1# test tube), this test tube is placed in the water bath of temperature 40 ℃ (that is, absorption temperature is 40 ℃); Take 10.0g water and place in another In a test tube (2# test tube), the test tube is also placed in a water bath with a temperature of 40°C; the simulated flue gas (mixed gas of nitrogen and sulfur dioxide) with a sulfur dioxide concentration of 1970ppm (volume fraction) is first bubbled through 2# The water in the test tube is bubbled through the absorbent of 1# test tube, and the flow rate of simulated flue gas is 100mL / min to absorb sulfur dioxide. After the absorption is saturated, adopt the iodometric method to measure the content of sulfur dioxide in the absorption liquid (see Example 1 for the measurement method); the measurement result shows that the absorption of sulfur dioxide in the absorbent is 0.0446g / g absorbent.
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