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By R. A. F. Williams

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14 days ^ ^ \ , 1 I 1 1 Height (mm) Fig. 9 g/1 hydroxyethylcellulose. Volume fraction,^, versus height of column (mm). 5 Rheological Measurements Rheological measurements were performed using a Bohlin VOR rheometer for controlled shear rate experiments, and a Bohlin CS rheometer for controlled stress (zero shear rate) experiments (Bohlin Reologi, Lund, Sweden). 3. 1 Non-adsorption of Added Polymer The electron spin resonance spectra of washed particles that had previously been equilibrated with spin labelled HEC, showed no evidence of any adsorbing polymer (Wedlock).

7. J. A. Hamza, Application of flocculants in hydrocyclone separation, Can. Instn. Min. Metall. , 66 (1973) 78-85. 32 1 Stream ΔΡ 50 70 90 10 Q 1 /m s~ U 0 F F* U 0 F F* U 0 F F* 6 . 83 /kg nr 3 /g 6 5 dm~ Wt. 5 29. 9 — 82. 9 - 100. 46 22345 20358 22345 1 0 0 . l); column 8 relates to performance of a single hydrocy clone, columns 1-6 refer to 6 x hydrocyclones in the manifold unit, Figure 2). 72 - Γ 8 12874 15400 12874 Body Re == 4 3 6 8 100. 0 — 7 aggregate unit. ^ 8. F. J. Brinson, Chemical Engineering, 62(2),234-238.

Direct observation of free-liquid formation in concentrated suspensions is probably a poor guide to dilatant sediment formation. 2 polymer concentration (g/1) Fig. 9 Zero shear viscosity as a function of free succinoglycan concentration for sterically stabilised 40 % v/v cyanazine dispersions. 98). 62 The results with non-adsorbing biopolymers, xanthan and succinoglycan, show the predicted influence of polymer molecular volume (intrinsic viscosity) on both the point of onset and the degree of flocculation.

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