摘要
Upon the application of 3%yeast suspension as a feedstock to an expanded bed of Streamline AC equilibrated with 0.02 mol·L -1 phosphate buffer (pH 7.0), the transient variations of local bed voidage and particle size distribution were investigated. The experiments were carried out in a customized glass column (26 mm I.D.) modified by side ports. It was exhibited that the introduction of unclarified feedstock with a high viscosity and density induced the upward movement of particle and consequently a change in local bed voidage and particle size distribution. At a given bed height, voidage firstly decreased to a minimum and then increased to a high equilibrated value in voidage. The transient process not only included a fluctuation in particle size distribution but also involved the change in particle concentration at a certain bed height, particularly at the middle and top of the column.
Upon the application of 3 % yeast suspension as a feedstock to an expanded bed of Streamline AC equilibrated with 0.02 mol · L^-1 phosphate buffer (pH 7.0), the transient variations of local bed voidage and particle size distribution were investigated. The experiments were carried out in a customized glass column (26 mm I.D. ) modified by side ports. It was exhibited that the introduction of unclarified feedstock with a high viscosity and density induced the upward movement of particle and consequently a change in local bed voidage and particle size distribution. At a given bed height, voidage firstly decreased to a minimum and then increased to a high equilibrated value in voidage. The transient process not only included a fluctuation in particle size distribution but also involved the change in particle concentration at a certain bed height, particularly at the middle and top of the column.
出处
《化工学报》
EI
CAS
CSCD
北大核心
2006年第2期371-375,共5页
CIESC Journal
基金
国家自然科学基金项目(20025617).~~
关键词
膨胀床
空隙率
粒径分布
酵母悬浮液
动态行为
expanded bed adsorption
bed voidage
particle size distribution
yeast suspension
transient phenomena