过程工程学报
過程工程學報
과정공정학보
The Chinese Journal of Process Engineering
2010年
1期
17-22
,共6页
磨损%颗粒%流化床%固定床
磨損%顆粒%流化床%固定床
마손%과립%류화상%고정상
attrition%particles%fluidized bed%fixed bed
在直径50 nm的冷模流化床与同定床耦合反应器中,考察了活性炭颗粒在130~150℃及不同气速下的磨损情况,得到了不同气速下固定床中圆柱状颗粒的磨损率随时间的变化关系,同时分析了滞留在流化床、固定床及袋滤器中的细颗粒在不同气速下的粒径分布与质量分布.结果表明,颗粒在该耦合反应器中磨损严重,在0.212~0.424m/s气速下,固定床中颗粒质量损失可达3%~4%,流化床中颗粒平均粒径由200μm降至100μm以下.
在直徑50 nm的冷模流化床與同定床耦閤反應器中,攷察瞭活性炭顆粒在130~150℃及不同氣速下的磨損情況,得到瞭不同氣速下固定床中圓柱狀顆粒的磨損率隨時間的變化關繫,同時分析瞭滯留在流化床、固定床及袋濾器中的細顆粒在不同氣速下的粒徑分佈與質量分佈.結果錶明,顆粒在該耦閤反應器中磨損嚴重,在0.212~0.424m/s氣速下,固定床中顆粒質量損失可達3%~4%,流化床中顆粒平均粒徑由200μm降至100μm以下.
재직경50 nm적랭모류화상여동정상우합반응기중,고찰료활성탄과립재130~150℃급불동기속하적마손정황,득도료불동기속하고정상중원주상과립적마손솔수시간적변화관계,동시분석료체류재류화상、고정상급대려기중적세과립재불동기속하적립경분포여질량분포.결과표명,과립재해우합반응기중마손엄중,재0.212~0.424m/s기속하,고정상중과립질량손실가체3%~4%,류화상중과립평균립경유200μm강지100μm이하.
The cold model experiments on the attrition of activated carbon particles were conducted in a steel-made coupled fluidized and fixed bed reactor with a diameter of 50 mm at 130~150℃. The relationship between the weight loss of particles (4.2 mm in diameter, cylinder-like particles) at the fixed bed section and gas velocity was analyzed. The free particles (0.2 mm in average size, pristine) of fluidized bed reactor, remained in the fluidized bed, fixed bed and the filter after fluidization, were s.tudied thoroughly to understand their profiles of particle size and their mass ratio in different positions under different gas velocities. It was found that the attrition of particles was serious. Under the high gas velocity (0.212~0.424 m/s), the weight loss of particles in the fixed bed was 3%~4%, and the mean size of fine particles in the fluidized bed was reduced from 200 μm to below 100 μm.