Citrus Research and Education Center, Univ. of Florida, Lake Alfred, FL, 33823, USA.
Dept. of Food Science and Technology, Univ. of Georgia, Athens, GA, 30602, USA.
J Food Sci. 2021 Jan;86(1):86-94. doi: 10.1111/1750-3841.15554. Epub 2020 Dec 16.
The characterization of the rheological properties of orange pulp under typical processing temperatures is needed for the design and optimization of orange pulp processing systems. The flow of orange pulp produced slip at shear rates at ∼1 to 5 s . Rotational rheometry revealed that the flow behavior of orange pulp before slip occurrence followed the Power Law model for concentrations of ∼500 to 800 g/L at 4 to 80 °C. The consistency coefficient (K) ranged from 33 to 234 Pa·s and the flow behavior index n ranged from 0.18 to 0.24. Both, K and n decreased with temperature. While K fitted well an Arrhenius-like model, n best fitted a linear model. As concentration increased K increased linearly, while n was not significantly (P > 0.05) affected. The flow without slip was calculated using the Power Law parameters from rotational rheometry and the wall shear stress (σ ) from capillary rheometry for the experimental flow rates. This allowed calculating the corrected slip coefficient β and obviated the need for pipes with multiple diameters. β decreased by one order of magnitude when temperature increased from 4 to 50 °C when σ was 0.1 kPa. The effect was exacerbated with increased flow rate. Similarly, β increased by about one order of magnitude when pulp concentration increased from ∼550 to 850 g/L at 80 °C. The increase in β with temperature indicated that the effect of temperature in the consistency of the bulk was different from its effect on the consistency of the liquid phase near the pipe wall. PRACTICAL APPLICATION: Design and optimization of processes equipment and industrial handling systems of orange pulp require detailed knowledge of their rheological (flow) properties. Citrus pulp like fruit pastes and purees produce less friction than one would anticipate when they flow because the liquid fraction acts as a lubricant. This study presents an original method for such characterization and shows that wall slip is greatly affected by temperature and concentration.
为了设计和优化橘子浆加工系统,需要对典型加工温度下的橘子浆流变特性进行描述。剪切速率约为 1 到 5 秒时,橘子浆产生流动。旋转流变仪表明,在滑动发生之前,橘子浆的流动行为在 4 到 80°C 时,浓度约为 500 到 800g/L 时符合幂律模型。稠度系数(K)范围为 33 到 234Pa·s,流动行为指数 n 范围为 0.18 到 0.24。K 和 n 都随温度降低而降低。虽然 K 很好地符合阿伦尼乌斯模型,但 n 最好符合线性模型。随着浓度的增加,K 呈线性增加,而 n 没有明显影响(P>0.05)。无滑动流动是通过旋转流变仪的幂律参数和毛细管流变仪的壁面剪切应力(σ)计算出来的,用于实验流量。这允许计算校正的滑动系数β,并避免了需要使用多直径的管道。当 σ 为 0.1kPa 时,温度从 4°C 升高到 50°C,β降低了一个数量级。当流速增加时,这种影响会加剧。同样,当 80°C 时 pulp 浓度从约 550 增加到 850g/L 时,β增加了约一个数量级。β随温度的增加表明,温度对整体稠度的影响与对管壁附近液相稠度的影响不同。实际应用:设计和优化橘子浆加工设备和工业处理系统需要详细了解其流变(流动)特性。柑橘浆等水果糊和果泥的流动摩擦力比人们预期的要小,因为液相部分起到了润滑剂的作用。本研究提出了一种用于此类特性描述的原始方法,并表明壁面滑动受温度和浓度的影响很大。