史德芳, 范秀芝, 殷朝敏, 姚芬, 冯翠萍, 程世伦, 高虹. 基于能耗分析的真空冷冻干燥食用菌汤块制备中试[J]. 农业工程学报, 2021, 37(10): 253-260. DOI: 10.11975/j.issn.1002-6819.2021.10.030
    引用本文: 史德芳, 范秀芝, 殷朝敏, 姚芬, 冯翠萍, 程世伦, 高虹. 基于能耗分析的真空冷冻干燥食用菌汤块制备中试[J]. 农业工程学报, 2021, 37(10): 253-260. DOI: 10.11975/j.issn.1002-6819.2021.10.030
    Shi Defang, Fan Xiuzhi, Yin Chaomin, Yao Fen, Feng Cuiping, Cheng Shilun, Gao Hong. Pilot-plant test of mushroom instant soup by vacuum freeze drying based on energy consumption analysis[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2021, 37(10): 253-260. DOI: 10.11975/j.issn.1002-6819.2021.10.030
    Citation: Shi Defang, Fan Xiuzhi, Yin Chaomin, Yao Fen, Feng Cuiping, Cheng Shilun, Gao Hong. Pilot-plant test of mushroom instant soup by vacuum freeze drying based on energy consumption analysis[J]. Transactions of the Chinese Society of Agricultural Engineering (Transactions of the CSAE), 2021, 37(10): 253-260. DOI: 10.11975/j.issn.1002-6819.2021.10.030

    基于能耗分析的真空冷冻干燥食用菌汤块制备中试

    Pilot-plant test of mushroom instant soup by vacuum freeze drying based on energy consumption analysis

    • 摘要: 为了降低冷冻干燥过程中能耗、推动冻干技术在食品中的应用,该研究应用在线调控预冻-冷冻干燥一体化设备进行食用菌汤块制备中试研究。对实际生产中冻结阶段(预冻温度、装盘物料厚度)、升华阶段(干燥仓压强、加热板温度)、解析阶段(水分转换点、升温工艺)等工艺进行了试验分析及优化,得出了适宜食用菌汤块冻干的节能工艺条件。提出了解析阶段的分步阶段升温法,并对解析阶段冻干曲线进行了拟合分析。结果表明,预冻温度设定为-35 ℃,装盘物料厚度为15 mm,干燥仓压强为25 Pa,汤块含水率为83.1%;升华阶段加热板温度为-10 ℃,解析阶段起始点为1 148 min,汤块含水率为9.2%,解析阶段采用分步阶段升温工艺(-10 ℃→2.5 ℃(70 min)→15 ℃(70 min)→27.5 ℃(70 min)→40 ℃(144 min))为较优选择,在此条件下,制备的汤块成品率为99.2%,感官品质指标综合分值为8.37,能耗为1.75 kW·h/kg,汤块含水率为4.3%。Boltzmann模型能较好表征解析阶段的冻干过程。该研究为冻干过程参数优化和能耗分析提供参考,为冻干技术应用于方便食品开发提供了技术依据。

       

      Abstract: Abstract: Mushroom instant soup is one of the most popular snack products in the diet of modern consumers. The typical consumption pattern is dramatically ever increasing for ready-to-eat, convenient, and cheap snacks, especially in most developing countries. The high-class mushroom can also provide delicious taste and abundant nutritive value. However, it has not yet been fully investigated how to develop instant soup with rich flavor and nutritional value.Compared with other preparation methods, freeze drying is commonly recognized to allow obtaining a higher quality product which can be easily rehydrated and retain organoleptic properties. In general, freeze-drying allows the dehydration of materials by sublimation at low temperature and sub-atmospheric pressure, thereby retaining higher nutritional value, flavor, color, and creating a porous structure in the dried products, all of which are desired attributes of dried products. However, freeze-drying is a typical high-energy-consuming operation, due mainly to the necessity of freezing products, heating the frozen samples to induce sublimation and lowering the total pressure of the dehydration chamber. As a result, freeze-drying in the food industry is restricted only to be applied in high-value-added products. Therefore, many attempts have been made to modify and optimize the whole drying process in order to extend the application fields of freeze-drying. A variety of products has been investigated on freeze drying using various theoretical models. Currently, the specific freeze- drying process can be simulated in many different approaches. An appropriate drying model needs to define the coordinate system, space dimensions, sublimation interface type, meshing technique, parameters variations over time and of time discretization. As such, various process variables can be used to evaluate the efficiency of the freeze-drying process, in terms of productivity and product quality (obtaining the highest quality in the shortest cycle time), especially in large scale production. Additionally, it is also highly required that the optimization should be implemented in-line pilot scale. In this study, a pilot plant test was conducted to investigate the energy-saving preparation of mushroom instant soup with an online regulation integrated freeze-drying. The operation parameters were analyzed to obtain optimal operation conditions, including the freezing stage (freezing temperature, thickness of loaded soup), sublimation stage (drying chamber pressure, heating temperature), and desorption stage (moisture conversion point, heating process). Especially, step-by-step heating was proposed and the freeze-drying curve was fitted in the desorption stage. The results showed that an optimal combination of parameters was achieved, where the pre-freezing temperature was set at -35 ℃, the thickness of loaded soup was 15 mm, the drying chamber pressure was 25 Pa, and the water content of the soup was 83.1%; the temperature of the heating plate in the sublimation stage was -10 ℃, the starting point in the desorption stage was 1 148 min (at this time, the moisture content of mushroom instant soup was 9.2%), and the heating (-10 ℃ → 2.5 ℃ (70 min) → 15 ℃ (70 min) → 27.5 ℃ (70 min) → 40 ℃ (144 min)) in the desorption stage. In this case, the the yield was 99.2%, overall score for sensory quality indicator was 8.37±0.52, the energy consumption was 1.75 kW·h/kg, and the water content of soup was 4.3%. Additionally, the fitting results of freeze drying curve during desorption stage showed that the Boltzmann model was well fit with the freeze-drying process in the desorption stage. The finding can provide a sound reference and technical support to the parameters optimization and energy consumption on the freeze-drying, particularly for the application of freeze-drying in the production of modern convenient food.

       

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