Martins Mayara Galvão, da Silva Pena Rosinelson
Graduate Program in Food Science and Technology, Technology Institute, Federal University of Pará (UFPA), Belém, PA 66075-110 Brazil.
Faculty of Food Engineering, Institute of Technology, Federal University of Pará (UFPA), Rua Augusto Corrêa 01, Belém, PA 66075-110 Brazil.
J Food Sci Technol. 2017 Sep;54(10):3170-3179. doi: 10.1007/s13197-017-2755-9. Epub 2017 Aug 8.
The osmotic dehydration (OD) and complementary drying of pirarucu () fillets were studied. Pieces of the dorsal portion of pirarucu (60 mm × 20 mm × 10 mm) underwent OD in a binary solution (NaCl-water) with the application of vacuum pulse following a central rotatable composite design. The effect of the following process variables was assessed: temperature (20-40 °C), osmotic solution concentration (15-25% NaCl), and vacuum pulse pressure (7-101 kPa) on water loss (WL), solid gain (SG), and water activity (a). OD kinetics was obtained and the Peleg model was fitted to WL and SG data. The osmotically dehydrated pirarucu was dried (40-70 °C) in a fixed-bed dryer and mathematical models were fitted to the drying data. The optimal operational condition for the OD process was 35 °C, solution with 25% NaCl, and atmospheric pressure, which yielded WL of 14.87 ± 1.46%, SG of 8.56 ± 0.45%, and a of 0.87 ± 0.02. The Peleg model efficiently predicted the WL and SG kinetics. The increase in the water loss in drying was more evident at low temperatures (40-50 °C) with effective diffusivity ranging from 10.85 × 10 to 12.30 × 10 m/s. The Midilli and Page models efficiently predicted the drying kinetics.
对巨骨舌鱼鱼片的渗透脱水(OD)及辅助干燥过程进行了研究。将巨骨舌鱼背部切成尺寸为60毫米×20毫米×10毫米的鱼片,按照中心旋转复合设计,在二元溶液(氯化钠 - 水)中进行OD处理,并施加真空脉冲。评估了以下工艺变量对水分损失(WL)、固形物增益(SG)和水分活度(a)的影响:温度(20 - 40°C)、渗透溶液浓度(15 - 25%氯化钠)和真空脉冲压力(7 - 101千帕)。获得了OD动力学数据,并将佩莱格模型拟合到WL和SG数据上。将经渗透脱水的巨骨舌鱼在固定床干燥器中进行干燥(40 - 70°C),并将数学模型拟合到干燥数据上。OD过程的最佳操作条件为35°C、25%氯化钠溶液和大气压,此时水分损失为14.87±1.46%,固形物增益为8.56±0.45%,水分活度为0.87±0.02。佩莱格模型有效地预测了WL和SG动力学。在低温(40 - 50°C)下,干燥过程中水分损失的增加更为明显,有效扩散系数范围为10.85×10至12.30×10米²/秒。米迪利模型和佩奇模型有效地预测了干燥动力学。