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Bidirectional drying of baled hay with air recirculation and cooling

机译:通过空气再循环和冷却技术对打包好的干草进行双向干燥

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Twelve batches of 60 small rectangular hay bales were dried artificially in a prototype dryer with air heated at 60°C. Bales were dried according to four treatments: I) unidirectional flow with 50% air recirculation; II) bidirectional flow with 50% air recirculation; III) bidirectional flow with 50% air recirculation plus a 30-min cooling period; IV) bidirectional flow with 90% air recirculation plus a 30-min cooling period. Bidirectional flow was applied by reversing airflow direction once during adrying cycle after 2/3 of the planned propane gas had been combusted. There were two drying cycles, an A-drying period when 100% thermal efficiency was assumed (average time in dryer between 2.5 and 3.5 h) and a B-drying period when the actual efficiency of the previous drying cycle was assumed (average time in dryer between 3.9 and 5.1 h). There was no significant difference between the four airflow treatments in terms of moisture content reduction, bale mass reduction, and thermal efficiency. Overallfor 720 bales, the average moisture content was reduced from 24.0% initially at baling to 20.1 % after A-drying period, 15.8% after B-drying period, and 12.6% after six weeks of storage. On average, 35 L of propane were required to dry a tonne of hay (874 kg dry matter) from the initial moisture content of 24%. The average time in the dryer was 6.8 h. Average bale masses were 31.1 kg at baling, 29.6 kg after A-drying, 28.0 kg after B-drying and 27.0 kg after storage. The thermal efficiency averaged 41.6% during period A and 26.7% during period B. Treatment IV with high air recirculation and cooling tended to have higher thermal efficiencies (45.3 and 30.2% for A and B periods, respectively) than the three other treatments. High density bales dried significantly more slowly (p = 0.028) than low density bales in the range of 161 to 182 kg (dry matter)/m~3. Bales should therefore be grouped as much as possible in a homogeneous batch, both in terms of density and initial moisture. Moisture content distribution was very homogeneous within individual bales after a 10-week storage period. The dryer could produce high quality hay bales for the commercial market. However, further analysis and experimentation are required to determine the optimal conditions for air velocity and temperature, time of drying, and cycles of air inversions.
机译:在原型干燥机中,用加热到60°C的空气人工干燥12批60个小的矩形干草。根据四种处理干燥棉包:I)单向流动,空气再循环率为50%; II)双向流动,空气再循环率为50%; III)双向流动,空气再循环率为50%,冷却时间为30分钟; IV)双向流动,空气再循环90%,冷却时间为30分钟。在计划的丙烷气体的2/3燃烧后的干燥循环中,通过一次改变气流方向来施加双向气流。有两个干燥循环,假设热效率为100%的情况下为A干燥期(干燥机的平均时间为2.5至3.5小时),假定先前的干燥循环的实际效率为B干燥期(平均干燥时间为)。干燥时间在3.9至5.1小时之间)。在减少水分含量,减少草捆质量和热效率方面,四种气流处理之间没有显着差异。总共720包,平均水分含量从打包时的最初24.0%降低到A干燥期后的20.1%,B干燥期后的15.8%和储存六周后的12.6%。从24%的初始水分含量开始,平均需要35升丙烷来干燥一吨干草(874千克干物质)。干燥机中的平均时间为6.8小时。打包时的平均包质量为31.1 kg,A干燥后为29.6 kg,B干燥后为28.0 kg,储存后为27.0 kg。在A期平均热效率为41.6%,在B期平均为26.7%。采用高空气再循环和冷却的处理IV的热效率往往比其他三个处理更高(A和B期分别为45.3和30.2%)。在161至182 kg(干物质)/ m〜3的范围内,高密度棉包的干燥速度明显慢于低密度棉包(p = 0.028)。因此,无论是在密度还是初始水分方面,棉包都应尽可能均匀地分组。贮藏10周后,单个包中的水分含量分布非常均匀。该干燥机可以为商业市场生产高质量的干草。但是,需要进一步的分析和实验来确定空气速度和温度,干燥时间以及空气倒置周期的最佳条件。

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