1976
DOI: 10.1002/cjce.5450540303
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Mixing of viscoelastic fluids with helical‐ribbon agitators. I — Mixing time and flow patterns

Abstract: Batch mixing of viscous fluids with helical‐ribbon agitators in 2.4 liter and 13 liter vessels has been studied for agitator speeds up to 200 RPM. Seven different agitators of different dimensions were employed in this work. Mixing times were measured using a decoloration technique and circulation times were determined by the tracer bead method. In addition, velocity profiles were obtained from streak photographs using selective illumination of the vessel and PVC powder as tracer particles. It was found that t… Show more

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Cited by 99 publications
(51 citation statements)
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“…The torque acting on the agitator shaft was measured using a torquemeter whereas the rotational speed was measured using a tachometer. More detailed descriptions of the experimental setup and procedure are available elsewhere (Carreau et al, 1976;Yap et al, 1979). It is sufficient to add here that each power data point represents an average of several repeated measurements in order to minimize the experimental uncertainty; the torque measurement is believed to be reproducible within *2.0%.…”
Section: Experimental Studiesmentioning
confidence: 99%
“…The torque acting on the agitator shaft was measured using a torquemeter whereas the rotational speed was measured using a tachometer. More detailed descriptions of the experimental setup and procedure are available elsewhere (Carreau et al, 1976;Yap et al, 1979). It is sufficient to add here that each power data point represents an average of several repeated measurements in order to minimize the experimental uncertainty; the torque measurement is believed to be reproducible within *2.0%.…”
Section: Experimental Studiesmentioning
confidence: 99%
“…It can be easily seen from Table 1 that mixing times are always several times greater than the circulation times (Carreau et al, 1976;Guerin et al, 1984;Takahashi et al, 1989;Takahashi et al, 1994). Therefore, an attempt can be made to find a relationship between the values of  m and  c for the same type of impeller irrespective of its geometric parameters.…”
Section: Data Inmentioning
confidence: 99%
“…Another method to find Q d is to integrate the axial velocity profile obtained from measurements (Carreau et al, 1976;Tanguy et al, 1992). A circulation number K Q can be defined in terms of…”
Section: Introductionmentioning
confidence: 99%
“…The circulation number is affected by the geometry of the mixing system and the fluid properties (Curran et al, 2000;Carreau et al, 1976). The geometrical configuration of a mixer plays a significant role in determination of the mixing performance.…”
Section: Introductionmentioning
confidence: 99%