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School of Graduate Study Department of Chemical Engineering

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In general concentrates involve counter current extraction. The three defatted soy protein<br />

concentrate extraction methods are discussed as follows.<br />

a) Aqueous alcohol Process<br />

The preferred alcohol concentration is 60% by weight. Soy proteins appear to be least<br />

soluble in about 50% aqueous alcohol; their solubility increases on either side <strong>of</strong> that<br />

concentration. Excess water in the extraction solvent is to be avoided because <strong>of</strong><br />

additional energy costs for removal and because an extremely wet soy protein cake tends<br />

to agglomerate, clogging the process system. The aqueous alcohol removed by<br />

evaporation from the alcohol water soy soluble is recycled to the extraction step<br />

(Antonio, 2007).<br />

b) Acid wash process<br />

The acid wash process yields soy protein concentrate products with a relatively high NSI<br />

(about 65-75%) because severe denaturation steps are not introduced in the process and<br />

the proteins are neutralized before drying (Smith and Circle,1972).<br />

Figure 2.1: Soybean Proteins; Effect <strong>of</strong> pH on Solubility<br />

(Based on Smith and Circle, 1972)<br />

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