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Thermal Food Processing

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<strong>Thermal</strong> <strong>Processing</strong> of Vegetables 411<br />

and hardness of texture. The LTB also caused increase in gumminess and springness<br />

of canned sweet potato. 59<br />

Many vegetables are washed, blanched, comminuted, and converted to puree<br />

or paste. The puree/paste is considered a minimally processed food, as the product<br />

is sometimes acidified (approximate pH = 4.0) and pasteurized. These products<br />

retain color and flavor comparable to the fresh produce and are convenient to use.<br />

The rheological characteristics of these products change during thermal processing.<br />

Rheological parameters are significantly affected by process temperature. Pureed<br />

food behaves as a non-Newtonian fluid with yield stress and is pseudoplastic in<br />

nature. 119 The consistency index decreased with temperature, while the flow behavior<br />

index increased. Rheological parameters obtained from a controlled rate rheometer<br />

of some strained vegetable pureed foods during thermal processing are<br />

presented in Table 13.4. Among various rheological models, the Hershel–Bulkley<br />

model (Equation 13.19) adequately describes shear stress–shear rate data of vegetable<br />

purees. The presence of yield stress ( o) of pureed food indicates application<br />

of minimum force to initiate the flow of the product. Temperature has a significant<br />

effect on o, and the yield stress decreased with temperature: 119<br />

TABLE 13.4<br />

Rheological Characteristics of Strained Vegetable Puree<br />

Vegetable Type<br />

Carrot puree<br />

(7.4°Brix and<br />

pH 4.88)<br />

Pea puree<br />

(7°Brix and<br />

pH 5.92)<br />

Corn puree<br />

(14°Brix and<br />

pH 6.46)<br />

Sweet potato<br />

puree (11.2°<br />

and pH 5.27)<br />

Wax bean puree<br />

(5.1°Brix and<br />

pH 5.05)<br />

Temperature<br />

Range (°C)<br />

τ = τ + K( γ)<br />

Yield<br />

Stress (Pa)<br />

Consistency<br />

Index<br />

(Pa·sec n )<br />

Flow<br />

Behavior<br />

Index (–)<br />

(13.19)<br />

Apparent<br />

Viscosity at<br />

100 sec –1<br />

(Pa·sec)<br />

20–80 1.65–3.72 5.44–11.53 0.27–0.35 0.24–0.42<br />

20–80 1.25–1.83 1.12–1.35 0.36–0.44 0.11–0.14<br />

20–80 0.43–1.18 0.58–2.06 0.26–0.30 0.02–0.05<br />

20–80 1.46–2.66 0.77–1.20 0.38–0.43 0.06–0.09<br />

20–80 5.10–5.23 0.22–1.86 0.48–1.0 0.23–0.26<br />

Source: Unpublished work of J. Ahmed and H.S. Ramaswamy.<br />

o<br />

.<br />

n

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