东南大学学报(自然科学版)
東南大學學報(自然科學版)
동남대학학보(자연과학판)
JOURNAL OF SOUTHEAST UNIVERSITY
2009年
5期
1002-1007
,共6页
鲍静静%杨林军%颜金培%刘锦辉%宋士娟
鮑靜靜%楊林軍%顏金培%劉錦輝%宋士娟
포정정%양림군%안금배%류금휘%송사연
湿法烟气脱硫%细颗粒%脱除%蒸汽相变
濕法煙氣脫硫%細顆粒%脫除%蒸汽相變
습법연기탈류%세과립%탈제%증기상변
wet flue gas desulphurization%fine particles%removal%heterogeneous condensation
通过在脱硫塔进口烟气、塔内脱硫液进口上方添加适量蒸汽等措施,在湿法烟气脱硫(WFGD)系统中进行了利用蒸汽相变原理高效脱除细颗粒的试验研究.考察了采用CaCO_3, Na_2CO_3, NH_3·H_2O等3种不同脱硫剂时,WFGD系统对细颗粒的脱除性能及其脱硫剂、蒸汽添加量、液气比(体积比)、脱硫塔进口气液温差等的影响,并进行了添加蒸汽和喷雾化水的对比试验.结果表明,由于形成无机盐气溶胶细颗粒,采用CaCO_3, NH_3·H_2O脱硫剂时,WFGD系统对细颗粒的脱除效果明显差于Na_2CO_3脱硫剂;在WFGD系统中应用蒸汽相变原理可显著促进细颗粒的脱除,在蒸汽添加量为0.05 kg/m~3时,细颗粒数浓度脱除效率可增至60%~70%以上;液气比的影响与脱硫塔内是否存在蒸汽相变有关;提高脱硫塔进口气液温差有利于细颗粒脱除;烟气温度较高时,利用雾化液滴的蒸发替代添加蒸汽也能显著促进细颗粒的脱除.
通過在脫硫塔進口煙氣、塔內脫硫液進口上方添加適量蒸汽等措施,在濕法煙氣脫硫(WFGD)繫統中進行瞭利用蒸汽相變原理高效脫除細顆粒的試驗研究.攷察瞭採用CaCO_3, Na_2CO_3, NH_3·H_2O等3種不同脫硫劑時,WFGD繫統對細顆粒的脫除性能及其脫硫劑、蒸汽添加量、液氣比(體積比)、脫硫塔進口氣液溫差等的影響,併進行瞭添加蒸汽和噴霧化水的對比試驗.結果錶明,由于形成無機鹽氣溶膠細顆粒,採用CaCO_3, NH_3·H_2O脫硫劑時,WFGD繫統對細顆粒的脫除效果明顯差于Na_2CO_3脫硫劑;在WFGD繫統中應用蒸汽相變原理可顯著促進細顆粒的脫除,在蒸汽添加量為0.05 kg/m~3時,細顆粒數濃度脫除效率可增至60%~70%以上;液氣比的影響與脫硫塔內是否存在蒸汽相變有關;提高脫硫塔進口氣液溫差有利于細顆粒脫除;煙氣溫度較高時,利用霧化液滴的蒸髮替代添加蒸汽也能顯著促進細顆粒的脫除.
통과재탈류탑진구연기、탑내탈류액진구상방첨가괄량증기등조시,재습법연기탈류(WFGD)계통중진행료이용증기상변원리고효탈제세과립적시험연구.고찰료채용CaCO_3, Na_2CO_3, NH_3·H_2O등3충불동탈류제시,WFGD계통대세과립적탈제성능급기탈류제、증기첨가량、액기비(체적비)、탈류탑진구기액온차등적영향,병진행료첨가증기화분무화수적대비시험.결과표명,유우형성무궤염기용효세과립,채용CaCO_3, NH_3·H_2O탈류제시,WFGD계통대세과립적탈제효과명현차우Na_2CO_3탈류제;재WFGD계통중응용증기상변원리가현저촉진세과립적탈제,재증기첨가량위0.05 kg/m~3시,세과립수농도탈제효솔가증지60%~70%이상;액기비적영향여탈류탑내시부존재증기상변유관;제고탈류탑진구기액온차유리우세과립탈제;연기온도교고시,이용무화액적적증발체대첨가증기야능현저촉진세과립적탈제.
A novel process to remove fine particles with high efficiency by heterogeneous condensation in a wet flue gas desulphurization (WFGD) system is presented. A supersaturated vapor phase, necessary for condensational growth of fine particles, was achieved in the SO_2 absorption zone and at the top of the wet FGD scrubber by adding steam in the gas inlet and above the scrubbing liquid inlet of the scrubber, respectively. The condensational grown droplets were then removed by the scrubbing liquid and a high-efficiency demister. The results show that the effectiveness of the WFGD system for removal of fine particles is related to the SO_2 absorbent employed. When using CaCO_3 and NH_3 · H_2O to remove SO_2 from flue gas, the fine particle removal efficiencies are lower than those using Na_2CO_3 and water as result of the formation of aerosol particles in the limestone and ammonia-based FGD processes. The performance of the WFGD system for removal of fine particles is significantly improved for both steam addition cases, for which the removal efficiency increases with the increasing amount of added steam. Removal efficiency of fine particles can reach to more than 60% ~70% while the amount of added steam being 0. 05 kg/m~3. A high liquid to gas ratio is beneficial for efficient removal of fine particles by heterogeneous condensation of water vapor. Removal efficiency of fine particles increases with increasing gas-liquid temperature difference at WFGD inlet. High removal efficiency can also be obtained by atomized droplets evaporation in hot flue gas besides steam addition.