广东化工
廣東化工
엄동화공
GUANGDONG CHEMICAL INDUSTRY
2012年
3期
8-9,38
,共3页
蒋凯%叶世超%彭健%柳海刚
蔣凱%葉世超%彭健%柳海剛
장개%협세초%팽건%류해강
氨法脱硫:喷淋塔%吸收率
氨法脫硫:噴淋塔%吸收率
안법탈류:분림탑%흡수솔
ammonia desulfurization: spray tower: absorption rate
文章在喷淋实验塔中,研究了氨法烟气脱硫的特性。将空气和气态二氧化硫按一定比例混合后的气体作为模拟烟气,用氨水作为脱除二氧化硫的吸收剂,对模拟烟气的进气温度、进气浓度、气速、液气比以及吸收液的pH五个因素对脱硫率的影响进行了逐一考察,获得了各因素与脱硫率之间的关系,并得到较适宜的操作参数。实验结果表明:随着液气比和吸收液pH的增大,脱硫率增大。随着模拟烟气进气温度、进气浓度和气速的增大,脱硫率降低。其中温度因素对脱硫率的影响不明显。实验得到适宜的操作参数为:常温下,模拟烟气气速为2.0m/s,液气比为10,pH为6.4时,对浓度为2000mg/m^3的烟气操作,收率可维持在85%以上,并在理论上对各因素和脱硫率之间的内在联系作了理论分析。
文章在噴淋實驗塔中,研究瞭氨法煙氣脫硫的特性。將空氣和氣態二氧化硫按一定比例混閤後的氣體作為模擬煙氣,用氨水作為脫除二氧化硫的吸收劑,對模擬煙氣的進氣溫度、進氣濃度、氣速、液氣比以及吸收液的pH五箇因素對脫硫率的影響進行瞭逐一攷察,穫得瞭各因素與脫硫率之間的關繫,併得到較適宜的操作參數。實驗結果錶明:隨著液氣比和吸收液pH的增大,脫硫率增大。隨著模擬煙氣進氣溫度、進氣濃度和氣速的增大,脫硫率降低。其中溫度因素對脫硫率的影響不明顯。實驗得到適宜的操作參數為:常溫下,模擬煙氣氣速為2.0m/s,液氣比為10,pH為6.4時,對濃度為2000mg/m^3的煙氣操作,收率可維持在85%以上,併在理論上對各因素和脫硫率之間的內在聯繫作瞭理論分析。
문장재분림실험탑중,연구료안법연기탈류적특성。장공기화기태이양화류안일정비례혼합후적기체작위모의연기,용안수작위탈제이양화류적흡수제,대모의연기적진기온도、진기농도、기속、액기비이급흡수액적pH오개인소대탈류솔적영향진행료축일고찰,획득료각인소여탈류솔지간적관계,병득도교괄의적조작삼수。실험결과표명:수착액기비화흡수액pH적증대,탈류솔증대。수착모의연기진기온도、진기농도화기속적증대,탈류솔강저。기중온도인소대탈류솔적영향불명현。실험득도괄의적조작삼수위:상온하,모의연기기속위2.0m/s,액기비위10,pH위6.4시,대농도위2000mg/m^3적연기조작,수솔가유지재85%이상,병재이론상대각인소화탈류솔지간적내재련계작료이론분석。
The characteristics of the process in ammonia-based FGD system were studied in an experimental-size spray tower. Simulated flue gas was obtained by mixing air and SO2(I) in certain ratio. The absorbent for removing SO2 was ammonia solution. Influencing factors such as temperature, inlet concentration of SO2 in simulated flue gas, gas velosity, liquid-gas ratio and pH value of absorbent were disscussed separately, out of which we've drawn an accurate conclusion of relationship between absorption rate and each factor. According to the data we gained, the modified experemental operating conditions were obtained, which shows that absorption rate increases with liquid-gas ratio or pH value increasing ,but decreases with temperature, inlet SO2 concentration or gas velosity. The impact of temperature is not significant. The absorption rate of simulated flue gas at the concentration of 2000 mg/m3 is able to reach over 85 % when operating condition maintains steadily at normal atmosphere temperature with inlet velosity at 2.0 m/s, liquid-gas ratio at 10, pH value at 6.4, and a theoretical analysis about their internal interaction has been achieved.